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0, for to > r,, the ambient medium being assumed uniform at t,: au au -+-=o, a x ay
ao + uao+& a?
at -
a7
ax
ay
=y
V2U- --, 1 aPm Pr aY
+ u-aaxt +I&= K V2t, a,v U(X,0,“)= U(X,
0,T) = t(X ,
(3.9) CO, 7 )
-f,
= 0.
(3.10)
It is not in general possible at this point to specify other bounding conditions in the ambient medium. The nature of any such applicable conditions depends upon the many additional approximations to be made in (3.7) and (3.8). The four equations above are in terms of the four distributions u, u, t , and p m . They are written below in terms of their mean and disturbance components (the relation between p’ and t‘ is also given): U(X,
y , 7 ) = c ( X , )’)
+ U’(x,)’, T ) , V ( x , y , T ) =
c(x, J’)+v ’ ( x , Y,T) (3.1 1)
t ( x . y , ~ ) =i ( x , y ) + t ’ ( x , y , 7 ) , P m ( X t Y 1 7 ) = ~ m ( X , Y ) + P ~ ( X ,Y’T)?
P( X, y , 7 ) = ii( x, y ) + P’( x , y , 7 ) = P( X, y ) - Pr a t ’ .
(3.12) (3.13) (3.14)
240
B . Gebhart and R . L . Mahajan
When these are introduced into (3.6)-(3.9), we obtain (3.15)
(3.17)
=K
v2i+K V2t’.
(3.18)
These results are written in expanded form to make clear the nature and impact of the approximations that follow. These approximations will yield the Orr-Sommerfeld equations, in terms of a conventional boundary-layer solution. The collection of approximations may be classified as follows: 1. The base flow is taken as that resulting from the first-order boundarylayer theory formulation. 2. Only first-order or linear terms in the disturbance quantities u’, u’, t‘ are retained. 3. After approximations 1 and 2 are made, the base-flow quantities U and the x derivatives of ii and i are taken as zero, sometimes called a parallelflow approximation. 4. In the postulated disturbances, x independence is assumed.
Applying assumption 1, the following collection of equations obtained from the above four equations are the equations governing the base flow:
-+-=o, az ac ax
ay
(3.19) (3.20)
(3.21) These equalities eliminate all these terms from (3.15)-(3.18). Also eliminated there, as a result of conventional boundary-layer approximations, are all other effects expressed purely in base-flow quantities. These consist of pm,all purely base-flow terms in (3.171, and stream-wise second derivatives.
24 1
Buoyancy-Induced Flows
Approximation 2 amounts to a small disturbance magnitude or linear approximation. This in turn means, for example, that periodic disturbances will not generate either harmonics or mean flow components. By assumption 2, all terms involving any product of u’, d,and t’ and/or their derivatives are eliminated. Approximation 3 is an ad hoc one. A base flow and transport, ii, 5, and i, were postulated in (3.19)-(3.21). The value of G in the resulting solution is not zero. Nevertheless, 5 and the x derivatives of both E and i are next taken equal to zero in the disturbance equations that remain after approximations 1 and 2 are made. The principal result is that all remaining terms in 5 disappear. The residual equations then become as follows: (3.22)
+ ii- au‘ + 0’- a ij = u v 2u’+ g & f ax ay
au’ -
aT
1 -, ap:, Pr ax
(3.23) ( 3.24)
(3.25)
The internal consistency of this collection of approximations is considered in the general discussion of such approximations, which is the last section of this work. Equations (3.19) and (3.22) suggest a stream function $(x, y , T)=&(x, y)++’(x, y , ~ such ) that
E=+,,
-
-5=+,,
u’=+’L ’
-V’=#;.
(3.26)
The conventional base-flow similarity transformations, the governing equations, and the boundary conditions are given below for Pr (Prandtl number) of order 1 or less: &=YC(x)F(q),
(3.27)
q=yb(x),
+ ( q ) = ( f - t m ) / ( i o - t w ) = ( f - t,)/d(x),
~(x)=4(Gr,/4)”~= G,
d(x)=N,x”,
b ( x ) = G/4x,
G r , = ( gx3/.’)PT(i0-
tm),
F ” ’ + ( n +3)FF” - ( 2 n +2)( F’)*++=O,
+”+Pr[(n+3)F+’-4nF’+]=O, F’(O)= F(O)= I -+(O)=
6(x)=4x/G,
F’(00)=+(00)=0,
Ucx/v= G2/4.
(3.28) (3.29) (3.30) (3.31) (3.32) (3.33) (3.34)
242
B . Gebhart and R . L. Mahajan
The listed boundary conditions are for an impervious vertical surface beginning at x=O, in an isothermal and quiescent ambient medium. The characteristic transport distance and tangential velocity are S(x) and U,( x), respectively. The numerical solutions of these equations for various values of n have been obtained for a wide range of Prandtl numbers (see, for example, Ostrach, 1964; Gebhart, 1971). The form of disturbance equations (3.23)(3.24), along with (3.26), suggests forming a disturbance vorticity equation in 4’. Then, the remaining disturbance functions, 4‘ and t’, are similarly postulated, for any given disturbance mode, as follows: 4’(x, y , 7 ) = 61/,@exp[i(c+x- j7)],
(3.35)
t’(x,y,7)=d(x)sexp[i(&x-87)1,
(3.36)
a=
c+S=c+,S+ic+,S=2nS/X+ iai,S=a,+ia,,
p = j S / u, = j , S / uc.
(3.37) (3.38)
The dimensionless amplitude functions across the transport region, @(q) and s(v), are in general complex. The two disturbances, linked through their residence in mass, are taken to be of similar form. Disturbance behavior is assumed to be periodic in x at any give? time. The wavenumber is 6,. They are periodic in time at all x, since fl=2nf, where f is the frequency. Amplitude damping or growth is assumed spatial and exponential, in x, in terms of a,. Neutral stability is a,=O and downstream amplification occurs for a, < 0. At this point, approximation 4 is invoked, to yield the usual OrrSommerfeld equations. These equations are in terms of the disturbance amplitude functions @ and s. The first part of approximation 4 is that the amplitude functions depend only on 77, that is, that @=@(q) and s = s ( q ) . This is analogous to the base-flow approximation that )C and F depend only on 9. The second part of approximation 4 is that the x derivatives of each disturbance spatial amplification rate &, and the disturbance wave length A, or G,, are taken as zero. The first three of these measures, concerning @, s, and &,, are supported quite well by numerous accurate measurements, in several different vertical buoyancy-induced flows. However, these same data, along with optical visualizations, indicate that X varies appreciably downstream. In fact it must, since frequency f is constant in an analysis by frequency modes, whereas the vigor of the base flow is x dependent. These downstream effects may be much more severe in more complicated flows of different geometric and bounding conditions. The improvement of the analysis, in any of the four categories of approximation previously set forth, must be consistently done. Any improvement effort
Buoyancy-Induced Flows
243
must be cognizant of the total body of approximations and not merely an ad hoc or selective treatment. The formulation of a consistent scheme of improved approximation is set forth in Section IX for several vertical flows. Substitution of (3.35)-(3.38) into (3.22)-(3.26) yields the Orr-Sommerfeld equations, in terms of disturbance amplitude functions @(q) and s( q). These are given together with the boundary conditions characteristic of a quiescent ambient medium:
( ~ ' - p / ~ ) ( w ' - ~ *~q" -' @ = ( @ ' ' " - 2 ~ 2 ~ " + ~ 4 @ + ~ (3.39) 1)/i~c, (F'- /3/a)s -+'@=(s"
- a2s)/icuPr G ,
@( 00)=@'(00)=s(00)=0.
(3.40) (3.41)
Three other boundary conditions, at 9 =0, depend upon the particular flow under consideration. The equations contain five independent parameters a r ,a , ,p, Pr, and G. Also, F ( q ) and +(q) are dependent on Pr. Solutions amount to finding G( p ) for a ,= O as the neutral stability condition, or curve, on /3, G coordinates. Contours of constant amplification rate - aiare then found in the unstable region. For constant physical PUJS a PG 3 / x 2 . Connecting x to G , for the to frequency we have f a variation with x that is appropriate to any particular flow, we have a relation between /3 and G at constant physical disturbance frequency. Thus we may follow a given disturbance on p, G coordinates and find the change in its amplitude, in the manner of Dring and Gebhart (1968), as it is convected along in the flow to larger x (that is, G). This is the way the constant-frequency paths in Fig. 2 were constructed for different flows, even for a horizontal flow. A simpler interpretation of downstream amplification results if /3 is generalized differently as follows:
8=
Q=j&?Gm/Uc.
(3.42)
For an isothermal condition, n -0 in (3.28) and m = f. The cumulative downstream amplitude growth, for the neutral condition at x, or G,, for a given value off, is calculated as follows. If A , is the disturbance amplitude of the periodic two-dimensional disturbance as it reaches the x location of neutral stability and A, is the amplitude farther downstream, then A is defined by A,/A,=eA,
4A=-
lnaidG.
(3.43)
The neutral curve is A =O. Neutral curves and constant-amplification contours have been calculated for many buoyancy-generating processes, since the first calculations of neutral stability by Plapp (1957), Szewcyzk (1962), Kurtz and Crandall (1962), and Nachtsheim (1963). The kinds of stability planes reproduced
244
B . Gebhart and R . L. Mahajan
here are for a vertical surface dissipating a uniform heat flux q“, n = 4 in (3.28). Figures 3 and 4 are stability planes for Pr=0.733 and 6.7, respectively. However, the generalization in these figures is in terms of a flux Grashof number G* and a generalized frequency &?*defined as follows:
G* =5(Gr:/5)’I5,
Gr: =g&x4q”/kv2.
(3.44) (3.45)
Q* = p G * ‘ / 2 ,
Note that the characteristic transport distance 6 and tangential velocity U, for the uniform flux surface are 6=5x/G*,
(3.46)
U , x/ v= G*2/ 5,
Similar stability planes, for plane plumes and for combined buoyancymode flows, are given in subsequent sections. For the surface-generated flow upon which Figs. 3 and 4 are based, the apparent additional boundary conditions were given by Knowles and
4.0 3.5
t
0.5 I”j
1 0
I
I
3.00
1
I
400
I
I
600
I
I
800
1
I
1000
ti* FIG.3. Stability plane for Pr=0.733 showing measured disturbance frequency for the unstable laminar flow (open symbols) and for locally laminar portions of the flow in the transition region (partially or fully shaded symbols). The dashed line is a constant-physicalfrequency path. Data are from Mahajan and Gebhart (1979).
s
245 A
1.6
-
7
/
/7
I
0
=O
200
I
I
I
400
600
800
I
1000
I
I
1200
1400
G+ FIG.4. Stability plane for Pr=6.7 showing amplitude curves in the unstable region. The dashed line represents the path of a rapidly amplifying frequency. The measured disturbance frequency data are from Qureshi and Gebhart (1978).
Gebhart (1968) as
@(O)
= W ( 0 )= 0,
(3.47) s(0) = i s ’ ( O ) / p , Q( G*)3’4, where
0, the relative thermal capacity parameter, is Q= ( ~ r c ’ ~ / p C ~ ) ( g p ~ q ’ ’ / k v ~ ) ’ ’ ~ .
(3.48)
Thus s(0) is not taken as zero unless the surface is massive, that is, very large. Since this is usually the practical circumstance in air, Fig. 3 was calculated with s(O)=O. However, Fig. 4 is based on s’(O)=O. It is seen in Figs. 3 and 4, from the trajectories of the constant-physicalfrequency paths shown, in 52* that these flows are very sharply selective in their amplification characteristics. The disturbances are filtered for essentially a single frequency (characteristic frequency) as they are convected downstream. The experimental data, like the points seen on Figs. 3 and 4, strongly substantiate this prediction. Comparison of the A contours in Figs. 3 and 4 indicates that the selected value of Q* is Pr dependent. The collection of available calculated and measured behavior was assembled as in Fig. 5 by Gebhart and Mahajan
B . Gebhart and R . L. Mahajan
246
I
I
1
I
10-2
I
102
Pr
I
104
Flc. 5. Characteristic Frequency data for vertical natural convection flows. Large and small Prandtl number asymptotes and + data points are from Hieber and Gebhart (1971a, b). Other data: 0, Polymeropoulous and Gebhart (1967). 8. Eckert and Soehngen (1951); 0, Knowles and Gebhart (1969); v, Shaukatullah (1974); Godaux and Gebhart (1974): a. Jaluria and Gebhart (1974).
m,
(1975). The right-hand ordinate in D corresponds to the isothermal surface condition, n=O. The !eft-hand one, in 9*,is for uniform surface flux and is defined in (3.45). In Fig. 5 the asymptotic dependences shown at large and small Pr were inferred from Hieber and Gebhart (1971a, b). The crosses at intermediate values of Pr are derived from detailed stability planes for each specific Pr value. The data points shown in this range are seen to be in very good agreement with the calculations. The kind of remarkable agreement seen above, between linear stability theory and experimental results, has been found to extend also to other and much more subtle aspects of unstable flows and transport. Such success is not common across the broad range of such research in fluid flow. Perhaps the reason for such close agreement in these flows is that the disturbance amplification is so highly selective and thus is not heavily dependent on particular aspects of each specific physical situation. Subsequent sections will indicate other very interesting downstream consequences of this initial characteristic.
Buoyancy- Induced Flows
247
IV. Nonlinear Disturbance Growth The disturbances, when sufficiently weak, grow downstream as predicted by the linear stability theory. However, as the disturbances become large, nonlinear mechanisms arise and their development begins to deviate from these predictions. These mechanisms are of two kinds: the possibility of generating higher harmonics and the generation of secondary mean flow due to nonlinear interaction of two-dimensional and transverse disturbances. The possible effects of higher harmonics on the disturbance growth are difficult to conjecture. They are perhaps not even significant in the later stages preceding transition, since the available experimental data for flows subject to both natural and controlled disturbances strongly indicate that a simple sinusoidal form of the highly amplified disturbances is retained during these later stages. The generation of a secondary mean flow, on the other hand, has been found to play an important role in the breakdown of the flow from laminar to turbulence. It has been studied both analytically and experimentally. OF SECONDARY MEANMOTIONS A. CALCULATIONS
The theoretical treatment is due to Audunson and Gebhart (1976). Their analysis postulates a two-dimensional disturbance modulated by a standing transverse disturbance. The relative amplitudes of the two disturbance components are allowed to vary while their phase velocities and wavelengths are assumed equal. These last two assumptions are similar to those used by Benny and Lin (1960) and by Benny (1961) in the nonlinear analysis of Blasius flow. However, Stuart (1965) has shown that two- and three-dimensional waves are unequal near the neutral curve, and therefore presumably are not in the amplified region downstream. Similar objections to the assumption of synchronization of two- and three-dimensional waves in forced flow have been raised by Hocking et al. (1972). An uncertainty regarding this synchronization also exists in natural convection flows. On the other hand, measurements of Jaluria and Gebhart (1973), of controlled disturbance propagation in a buoyancy-induced flow, indicate that the velocities of the two waves are nearly the same (see Fig. 6). Their phases are, however, about one-quarter of a period apart. Nevertheless, the great simplicity of the analysis following the assumption of equality of phases, along with a posteriori good agreement between the predictions of the analysis and the experimental results, justifies the simplifying assumptions in the analysis. Retaining these postulated nonlinear interactions in the disturbance equations, finite amplitude effects were calculated by a systematic perturba-
B . Gebhart and R . L. Mahajan
248
(b)
(d)
FIG.6 . Two-dimensional and transverse velocity disturbance versus time as measured at various downstream locations: G' =350 (a). 400 (b). 500 (c). 545 (d). Upper signal for each G* is the transverse one (from Audunson and Gebhart 1976).
tion of linear stability theory. The nonlinear interaction of the solutions to the homogeneous Orr-Sommerfeld equations provides the driving functions for the first perturbation from linearized analysis. For details, the reader is referred to Audunson (1971). Numerical solutions were obtained for four base-flow conditions having very different linear stability characteristics, for Pr = 0.733. The flow conditions chosen are shown on the two-dimensional disturbance stability plane in Fig. 3. Points B, C, and D lie close to the path of most amplified frequency. D is at the neutral condition, whereas C and B are in the amplified domain. Point A is at the same value of G* as B but lies on the neutral curve. The results indicate a strong dependence of the resulting secondary flows on both G* and frequency Q*. For point B lying in the highly unstable region, a double longitudinal mean secondary vortex system is indicated (see Fig. 7). In Fig. 7 X,/X, is a measure of the relative strength of two-dimensional and transverse disturbances, B is the transverse wavenumber, and z is the coordinate in the transverse direction. The streamlines shown are for conditions of A,/& = 100 (highly two-dimensional disturbance) to A,/h,=O (a purely transverse oscillation). For h,/h,>> I (Fig. 7a) the streamlines indicate mean cellular vortex structure motion with spanwise periodicity of 2n/fl. With increasing three-dimensionality of the flow, i.e., decreasing A,/&, the centers of the outer rolls move toward spanwise locations 8z = 2ns, whereas the centers of the inner rolls are pushed towards spanwise locations 8z = ( 2 n 1)a (see Figs. 7b, c). For the extreme case of purely transverse primary oscillation, the vortex structure is shown in Fig. 7d. The spanwise period is a/O.
+
Buoyancy- Induced Flows
249
FIG. 7. The calculated streamlines of the mean secondary flow for point B in Fig. 3. Stream function value 0, O.oooO5: I , 0.0001; 2, 0.0002: 3. 0.0005; 4. 0.001: 5, 0.005: 6.0.01: 7.0.05; 8,O.l. G*=700;X,/h,= 100 (a). 2.0 (b). 0.2 (c), 0.0 (d) (from Audunson and Gebhart. 1976).
Such secondary motions imply a large momentum transport across the boundary region and result in important modifications of the mean flow. The result in Fig. 7a is of primary interest, since it closely represents the mainly two-dimensional flow preceding transition. At 8z = (2n + I)n the inner roll carries primarily high-momentum fluid from the inner part of the boundary layer to the outer slower-moving region. On the other hand, the counter-rotating outer vortex brings low-momentum fluid from the far field into the boundary region at this same z location. These cross flows result in steepening of the outer part of the mean velocity profile at locations 8z =(2n 1)s and flattening of it at locations Bz =2nn. Since energy transfer to a disturbance is at least approximately proportional to the velocity gradient, or shear, of the mean flow, the disturbance
+
250
B . Gebhart and R . L . Mahajan
growth rate is strongly augmented at 6z = (2n + 1)a locations, the regions of high shear. At Bz=2na locations, reduction in disturbance growth is suggested. Note that the calculated locations of high shear are just the opposite of those found in analogous Blasius forced flow. The quiescent far field, rather than the region near the surface, is the source of low momentum that causes the high-shear region. Further, in forced flows the presence of only a single-longitudinal-vortex system was detected (Klebanoff et al. 1962). These vortices occupied only the inner half of the boundary region. In the buoyancy-induced flows considered here, however, a double-vortex system is indicated and the outer vortices stretch across the boundary region, out into the quiescent fluid. These vortices may therefore be expected to cause a great distortion in the longitudinal mean velocity profile. Associated with these secondary flows is also an alternating spanwise modification of the mean temperature distribution across the boundary layer. At spanwise locations Bz = 2na the local heat transfer is augmented, whereas at 6z = (2n + 1)s a decrease occurs. The computed results for point C were shown to be in complete agreement with those discussed above for point B. This is not surprising since both points lie in the highly unstable regions and have the same physical frequency. However, it is of interest to see if the streamlines calculated for point D at the neutral curve, but along the same high-amplification path, show similar secondary flow characteristics. The results are shown in Fig. 8. For X,/X,= 10 one dominating outer roll is seen, but a weak inner circulation also begins. The general behavior at other values of A,/h, is the same as for the highly amplified flow at point B. Thus, along the highamplification path, a double-longitudinal-vortex system is produced at the earliest stages of instability and continues to be found in the region of highly amplified disturbances. Consider now the streamlines shown in Fig. 9 for point A, which is at the same value of G* as B but does not lie along the path of amplifying disturbances. The results are very different from those at point B. Only a single longitudinal roll results. Increase in three-dimensionality of the flow produces similar changes in the streamline pattern as for point B (Figs. 9b,c). The resulting modifications of the mean flow caused by highly two-dimensional oscillation (Fig. 9a) are also compatible with former results. Spanwise locations Bz = (2n + l)n experience a momentum defect in the inner and outer parts of the boundary layer, and at Oz=2nv the situation is reversed. Thus, there is again an alternating spanwise thinning and thickening of the boundary layer. However, this single-roll system does not appear to produce any significant steepening of the outer part of the velocity profile. The profile merely shifts in and out from the surface while
Buoyancy-lnduced Flows
25 1
FIG. 8. The calculated streamlines of the mean secondary flow for point D. Stream function value: I . O.ooOo5; 2. 0.0005: 3, 0.005: 4. 0.05: 5. 0.2: G*= 160: ?,,/A,= 10 (a), 0.2 (b). 0 (c) (from Audunson and Gebhart, 1976).
retaining its original form. These changes would not be expected to augment disturbance growth. From the above results, it appears that a double-vortex system is predicted at points D, C, and B, as the most highly amplified disturbance is convected downstream. Thus, the secondary mean flow configuration need
B . Gebhart and R . L. Mahajan
252
(b)
(C)
FIG. 9. The calculated streamlines of the mean secondary flow for point A. Stream function value: 0. O.OOO1; 1, 0.OOOS:2. 0.001; 3, 0.005; 4, 0.01; 5 , 0.05; 6 , 0.1; 7, 0.5; 8. I. G*=700; &/A,= 10.0 (a), 0.2 (b), 0.0 (c) (from Audunson and Gebhart, 1976).
not appreciably change as this disturbance is convected downstream. It merely enhances itself. This probably occurs simultaneously with the continued concentration of disturbance energy into the filtered twodimensional primary wave. In other words, linear and nonlinear mechanisms appear to proceed hand in hand in a highly filtered way. This important result is very different from what is observed in forced flows. It
Buoyancy-Induced Flows
253
would be interesting to calculate the integrated downstream effect of an initially three-dimensional disturbance along this filtered path and compare the results with the experimental measurements of the disturbance form and of transition.
B. MEASUREMENTS IN CONTROLLED EXPERIMENTS OF NONLINEAR GROWTH Excellent corroboration to these analytical results has been provided by the detailed experimental studies of Jaluria and Gebhart (1973). The measurements were in the flow adjacent to a vertical uniform flux surface, in water. Controlled two-dimensional disturbances, with a superimposed transverse variation, were introduced in the flow by a vibrating ribbon (see Fig. 1Oc). The input disturbances were introduced at location G*= 140. 0.06-
I
I
I
l
l
0.04 0.02
-w K C,
-
0-
-0.02 -
-0.04-
- 0.06 L
“I
0.8 0.6 1.0
“&ax
0.4
-
0.2
-
I
I
w: I
“
r -
I
1
I
I
I
I l
I
I I
I
I
1
l2.7mm
b-4
r n
l
l
I 1
MAX MIN MAX MIN 1 I , I
I
I
VIBRATOR
FOIL
Fw. 10. Configuration of vibrating ribbon and measured downstream spanwise distribution of u‘ and W. The measurements are at a single value o f each x and I’.
254
B . Gebhart and R. L. Mahajan
This lies well in the unstable portion of the stability plane (see Fig. 4). The resulting behavior of the disturbances, and of the mean flow downstream, was studied in detail. Recall that the actual local mean flow is the sum of the base flow ‘ii and E and any secondary mean flow that might arise through interaction among the disturbances and this base flow. Denoting the resulting mean flow components as U , V , and W, the resulting components of the secondary mean flow are U - U, V - V , and W. The periodic parts of the velocity components, as before, are u’, u’, and w’. In the first few experiments of Jaluria and Gebhart (1973), the frequency of the vibrating ribbon was varied at constant disturbance amplitude and measurements were made of the amplitude velocity disturbance u’, downstream at different x and z locations. The data indicated that the most rapidly amplifying frequency was almost exactly equal to that predicted by linear stability theory. The conclusion was that the frequency filtering mechanism discussed in Section I11 for boundary-layer flows subject to two-dimensional disturbances is not affected by a spanwise variation in the input disturbance. In subsequent experiments this frequency was chosen for the input disturbance. The data are in the range G* =400-600. The spanwise distribution of u’ normalized by the maximum value measured in the transverse direction z across the surface, is shown in Fig. lob. The initial spanwise positions of maxima and minima in u’ were found to be preserved downstream in a given flow, indicating more or less vertical propagation of the disturbance pattern. However, peaks and valleys are seen to be very sharp, quite unlike the input disturbance. This indicates that these measurements were taken in the region of amplifying transverse effects, which, through linear and/or nonlinear interactions, accentuate the ribbon input spanwise variation of u’. Other data indicated that, for smaller disturbance amplitudes, linear effects dominate. Nonlinear interactions arose at larger amplitudes. Associated with this spanwise variation of u’ is the variation of the transverse component W of the secondary mean flow across the boundary region (shown in Fig. 10a). Evidence of longitudinal rolls is seen in Fig. 11. The measured y distribution of W , normalized by Emax,the measured maximum velocity in the base profile without disturbances, is plotted against 7. These distributions indicate the changing form of W ( 7 )with G* (Fig. l l a ) and with z (Figs. I la, b). In each distribution, W changes sign twice across the boundary region. In Fig. l l a , W starts with negative values at low 9 , rises to a peak at positive W, and returns to negative values again before gradually dying out at large 9. The two sign reversals suggest the centers of two rolls, since W is in one direction on one side of each center and in the opposite
Buoyancy-Induced Flows
255
0.04
0.02 x
E 0
3 113
-0.02
-0.02t
1
- 0.04 -0.06
k
-0.061 ,
0
l
I
I
2
1
1
4
1
1
6
1
I
8
7 (b)
Fw. 1 I . Distribution of the transverse component W across the boundary region. ( a ) 0. G*=400 at z=86.36 rnm: 0. G*=460 at z=86.36 m m ( b ) A, G*=460 at r = 7 6 . 2 mm: A. G*=460 at z=78.74 rnm.
direction on the other. Assuming two rolls, the location of their interface is where W attains the highest absolute values. Since this occurs around TJ = 1.7, the inner roll extends from q = 0 to TJ = 1.7. The outer roll, on the other hand, stretches from q = 1.7 to q = 7 for G* = 400 and beyond for G*=460. The extent of the inner roll for these two G* values appears to be the same. The distribution in Fig. 1 Ib at z = 78.74 mm is just the opposite of that in Fig. 1la, at z = 86.36 mm. It starts at a positive value of W at low q, goes through two sign reversals, and dies out at small positive values at large TJ. This comparison, at two z locations at the same G*, indicates a plane of demarcation between these transverse locations. On the opposite sides of this plane, the vortices rotate in opposite directions. The minimum in the input disturbance, at z = 83.32 mm, is the most probable site of the location of this plane. The maxima and minima in the input disturbance are locations of symmetry. Zero mean transverse flow is expected at these locations. Similar reversal in form of these curves from z=73.66 to z = 69.45 mm (not shown in the figure) indicated t = 7 1.12 mm, the location of input disturbance maximum, as the plane of symmetry for the two counterrotating vortices. Thus, each pair of longitudinal vortices stretches in the transverse direction from positions of a maximum to a minimum in the input disturbance.
B . Gebhart and R . L. Mahajan
256
This is further confirmed by the measurements of W in the transverse direction (see Fig. 10). The component W reaches zero value at z=71.63, 83.31, and 96.27 mm, indicating that one vortex pair extends from z = 71.63 to z = 83.3 1 mm and that the adjacent vortex pair extends from z = 83.3 1 to approximately ~ 1 9 6 . 2 7 mm. Each vortex pair thus lies between a maximum and a minimum, located at z=83.32 and z=71.12 mm for the input disturbance. The slight difference is probably due to a shift of the vortex pattern caused by the hot wire sensors used to measure W. The total picture of the longitudinal vortex system that emerges from these measurements is shown in Fig. 12. The vortex pair lies between adjacent maxima and minima in the input disturbance. The inner roll is close to the wall, whereas the other stretches out across the boundary layer into the ambient medium. This double longitudinal vortex is in excellent agreement with the analytical predictions of Audunson and Gebhart ( 1976) (see, for example, Fig. 7a). Since the Prandtl number (Pr=6.7) in these measurements is different from that of the analysis (Pr=0.733), a quantitative comparison between the two is not relevant. However, the overall features are the same. At high Prandtl number one would expect the vortex system to be closer to the wall. These measurements in water, when compared with the theoretical vortex pattern in air, indicate that this
I I I I
a,
1 I I
I
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I I
I
I
I
I I
0
min
I
I I
1 I
I
I
I I
I I I
I I
l
max
- 2
FIG. 12. Sketch of the double mean longitudinal vortex system.
Buoyancy-Induced Flows
257
C. THEROLEOF MEANSECONDARY FLOWS
Such a double-longitudinal-vortex system results in a large momentum transport of downstream momentum across the boundary layer. At the location of a maximum in the input disturbance, the outer vortex tends to convect higher-velocity fluid outward in the boundary region. However, at a minimum, it brings fluid into the boundary region from the quiescent medium. The inner roll does just the opposite. The resulting mean flow velocity induced by these momentum transports is steepened around the inflection point at the spanwise position corresponding to a minimum. It is flattened at a maximum (see Fig. 13). Thus, there is an alternate spanwise steepening and flattening of the mean velocity profile, accompanied by an alternate thinning and thickening of the boundary layer. In the regions of
0
1
2
3
4
5
6
7) FIG. 13. Measured longitudinal mean-flow profiles. compared with that for undistributed flow. Data: 0 . at spanwise location of primary disturbance minimurn: 0. at spanwise location of primary disturbance maximum: B. undisturbed flow.
258
B . Gebhart and R . L . Mahajan
local steepening, the disturbance growth is augmented. The measurements indicate that with increasing G*,the spanwise distortion of the mean velocity profile increases. Consequently, augmentation of the disturbance growth becomes increasingly intense. These results are again in good agreement with the analysis of Audunson and Gebhart (1976). Prior to this analysis and to the conclusive corroborative experimental results of Jaluria and Gebhart (1973), there was some controversy concerning the role and the form of three-dimensional disturbances and of nonlinear mechanisms in natural convection flows. Colak-Antic (1962) had suspended highly reflective aluminum particles in water and observed their behavior during transition in the convective layer formed adjacent to a heated vertical flat surface. Two longitudinal vortices, similar to those predicted by the theory of Audunson and Gebhart, were seen. However, by dye visualization Szewczk (1962) observed vortices whose axes were transverse. The formation of a vortex loop was postulated, in which the vorticity field is considered to be concentrated. Although this hypothesis appeared to provide a plausible explanation for observed phenomena, there is some ambiguity in relating dye injection to vorticity concentration. Interestingly, a similar difference of opinion regarding such mechanisms arose in forced flows until Klebanoff et al. (1962) established, from detailed experiments with controlled three-dimensional disturbances, that secondary mean-flow longitudinal vortices occur as a consequence of nonlinear and threedimensional interactions. Additional explanations that have been offered are as follows: the generation of higher harmonics and the effects of the concave streamline curvature associated with the wave motion, in addition to the vortex loop formation. However, it is now reasonable to conclude that these effects do not dominate the overall behavior of transition and that regions of high shear, along with other consequences of the longitudinal vortex system, are associated with the onset of transition to turbulence.
D. NONLINEAR EFFECTS RESULTINGFROM NATURALLY OCCURRING DISTURBANCES Although the nonlinear growth mechanisms discussed above arose from artificially introduced disturbances, there is ample reason to believe that these effects also arise in flows subject only to naturally occurring disturbances. A frequent source of such disturbances, which arise from ambient disturbance sources, is through external vibration (see Tani, 1969, concerning forced flow). This mode of origin is very similar to that imposed by a vibrating ribbon in controlled experiments. There are, however, important differences. The artificial disturbances were introduced across the boundary region at one streamwise location x , beyond the neutral curve, in the
Buoyancy-Induced Flows
259
unstable region of the stability plane. Natural disturbances, on the other hand, may be fed in over the entire boundary region. Further, these disturbances contribute a spectrum of frequencies, as indicated by hot-wire measurements of background disturbances by Jaluria and Gebhart ( 1977). No dominant frequency was found. However, for any natural disturbances of a given amplitude, introduced at many different downstream locations, the one introduced.at the neutral stability condition would reach the highest amplitude downstream, since this disturbance would have had the longest path of amplification. Further, any such disturbance. with a broad range of component frequencies, is subject to selective amplification, or filtering, downstream. Therefore in the amplified domain the disturbance components that really count are those that are impressed at a location corresponding to the early stages of initial instability and that are at the most rapidly amplifying frequency. Thus, the end result for the two circumstances-of the introduction of disturbance through a vibrating ribbon at the most amplifying frequency near the neutral curve, or through a spectrum of naturally occurring disturbances across the entire boundary region-is expected to be the same. Available experimental data confirm this. Jaluria and Gebhart ( 1974) measured W in their investigation, in water, of transition mechanisms in natural convection flow, subject to naturally occurring disturbances. Its small magnitude and the random noise level made complete measurements impossible. However, the measured variation of W over a portion of the boundary layer is in good agreement with the distribution already shown in Fig. 11. The presence of longitudinal rolls is thus implied. The double longitudinal vortex observed by Colak-Antic (1964) is also for a flow subject only to naturally occurring disturbances, again confirming that the nonlinear interactions cause such mean flow modifications.
V. Transition and Progression to Developed Turbulence The previous sections discussed the sequence of events leading toward eventual transition. The laminar boundary layer becomes unstable to ever-present disturbances at some distance downstream. These first amplify in excellent agreement with the linear stability theory. Later the consequences of nonlinear interactions arise. A double longitudinal mean vortex is generated that, through the formation of regions of higher shear, contributes to rapid disturbance growth. These events, in broad outline, are similar to those observed in forced convection flows. However, the analogy ends here. In forced flows it is thought that the high-shear region, acting as a secondary instability, generates rapidly oscillating “hairpin eddies.” These
B . Gebhart and R . L. Mahajan
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are produced intermittently in the boundary layer and immediately precede the formation of turbulent spots. On the other hand, the process of transition in natural convection flows is long drawn out and also more complicated. The velocity and temperature fields in natural convection flows are coupled together, and this has been found to cause significant additional effects on transition mechanisms in such flows. The way the two fields interact and influence each other is also Pr dependent, which in turn, then, becomes an additional parameter. Most studies of transition in natural convection flows have been in the two most common fluids in nature: water (Pr=i6.7) and air (Pr-0.7). Although the overall transition mechanisms in these fluids appear quite similar, some important differences are apparent. A brief review of what is known of transition in these fluids follows.
Developed Turbulence Laminar 1.2 BoundaryRegion Thickness
Turbulent Cascade to Smaller Scoies BL -I I
1.0
!
x(m1 0.81
0.6
I ,
Transition Proceeds
L
T, . / !
0.4
, Y ~ T ,Mean Flow Deviation Begins
FIG. 14. The sequence of downstream events during transition in water from a stable laminar flow to full turbulence. The spatial extent of each regime is shown to scale for a uniform flux surface condition of q ” = 1000 W/m2. G:, neutral stability for most rapidly amplified disturbance; GtT and G k , beginning of velocity and thermal transition, respectively; G&, end of transition.
Buoyancy-Znduced Flows
26 1
In water, to date, the most detailed investigations of transition mechanisms are by Godaux and Gebhart (1974), Jaluria and Gebhart (1974), and Qureshi and Gebhart (1978). Prior investigations (e.g., VIiet and Liu, 1969; Lock and Trotter, 1968, deal primarily with turbulent flows, although a few measurements during transition are also reported. An overall picture of transition that emerges from these studies is shown in Fig. 14. The turbulent disturbances first occur in the thicker velocity boundary layer. These apparently then cause the first signs of turbulence inside the thermal boundary layer. Further downstream, the maximum value of the base-flow velocity begins to decrease from its laminar trend. Simultaneously, the mean velocity profile also deviates from its laminar form. This is the beginning of velocity transition. The velocity disturbances then become strong enough to diffuse the thermal layer material into the outer velocity layer. This begins a change in the mean temperature profile-the beginning of thermal transition. As transition progresses, the velocity and thermal boundary layers mix and thicken, and the mean profiles deviate progressively from the corresponding laminar ones. The end of transition is simultaneously marked by no appreciable further change in the distributions of local velocity and temperature intermittency factors 1, and Z,. These factors, I, and 1,,are defined as the fraction of the time the flow at any point is turbulent, in the velocity and temperature values, respectively. The end of transition (see Bill and Gebhart, 1979) is followed by a regime of spectral and transport development. The spectrum of velocity fluctuations broadens and temperature fluctuations decrease in magnitude. Also, the turbulent heat-transfer mechanisms become more effective, despite the leveling of the growth of velocity disturbances. This development process continues downstream, until the distributions, scales, intensities, and other turbulent parameters largely adjust to the final characteristics of the turbulent flow. In gases, some data in the transition regime are available from the experimental studies of turbulent flow by Regnier and Kaplan (1963), Cheesewright (1968), Warner (1966), Warner and Arpaci (1968), and Smith (1972). A detailed determination of transition mechanisms in gases is provided by experiments of Mahajan and Gebhart (1979), in a vertical natural convection flow adjacent to a uniform heat-flux surface in pressurized nitrogen. These measurements indicate that the overall mechanisms are similar to those in water. The thermal transition follows velocity transition. However, since the two boundary layers are of comparable thickness, as opposed to water in which the thermal boundary layer is well contained in the velocity boundary layer (Prandtl number effect), the disturbance fluctuations in velocity more quickly affect the temperature boundary region. Both the velocity and thermal transitions are thus triggered almost simultaneously.
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The region of spectral development beyond the end of transition, to the achievement of developed turbulence, has not been systematically studied in air. However, the experimental data reported by Smith (1972) in his study of turbulent flow adjacent to an isothermal plate in air indicate, unlike in water, no well-defined region of adjustment of turbulent-flow parameters. The reason for this difference can probably again be traced to Prandtl number effect. In water, the lag in the development of temperature disturbance levels observed in the early stages of transition continues until the end of transition. Thus, the spectral region may be looked upon as the regime in which temperature disturbances must catch up with the velocity disturbances. In air, however, the velocity and temperature disturbances develop equally side by side, from the beginning to the end of transition. Before beginning a detailed description of the stages of transition, in both air and water, a few remarks about the definition of the beginning and end of transition are in order. Although the criterion described above, to define end of transition, seems to have been successfully used for both liquids and gases, a multiplicity of criteria have been used in the past to mark the beginning of transition. Further, excepting the recent studies, no distinction seems to have been made between a velocity and a thermal transition. The beginning has been said to be signaled by the presence of significant temperature fluctuations, an increase in heat transfer effectiveness from the laminar trends, a decrease in temperature difference across the boundary layer from its laminar value for a uniform flux condition, and a deviation from laminar mean temperature profile. These are the most commonly used criteria to indicate the beginning of what is now known as thermal transition. Mahajan and Gebhart (1979) found that the events upon which the last three criteria are based occur almost simultaneously. Here, these criteria have been used interchangeably, although Mahajan and Gebhart found that a decrease in AT, the temperature difference across the boundary layer, from the calculated laminar value is a sharper indicator than others to define the beginning of thermal transition. The beginning of velocity transition, first studied in detail by Jaluria and Gebhart ( 1 974) in water, was indicated by the presence of a higher-frequency component superimposed on the single laminar filtered frequency. However, in gases, Mahajan and Gebhart (1979) found that this criterion could not be used unambiguously. Instead, deviation of U,,, , the observed local maximum value of the tangential flow velocity across the boundary region, from its laminar trend downstream was used to mark the beginning of velocity transition. In the experiment of Jaluria and Gebhart (1974) in water, this event occurs downstream of their designated location of the beginning of transition. The criterion of Mahajan and Gebhart (1979) is now used as the indicator of beginning of transition because of its precision and applicability to both liquids and gases.
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263
A. TRANSITIONAL MEANVELOCITYAND TEMPERATURE DISTRIBUTIONS
Figure 15 shows the velocity measurements of Mahajan and Gebhart (l979), in nitrogen, at several values of q", in laminar flow and in transition. The downstream distance x was 22 cm and the ambient pressure of N, was 8.36 atm. From these data, the values of G* at the beginning of velocity transition, the beginning of thermal transition, and the end of transition (G&, G&, and Gg,) are 450, 480, and 61 1, respectively. In Fig. 15a, measured distributions of U , normalized by the maximum value U,,, found across the boundary layer, are plotted versus the laminar similarity variable 7). The measured values of U,,, normalized by local calculated laminar values, Urnax,at the same conditions are plotted in Fig. 15b. At G* =434, the measured value of U,,, and the mean velocity profile are in good agreement with the calculated laminar values. However, at G*= 470, which is downstream of the beginning of velocity transition, U,,, is about 4% below the laminar value and the mean profile has begun to deviate. As transition progresses, the deviations in form increase. The flow penetrates deeper into ambient medium as a consequence of growing turbulence in the boundary region. As the flow region thickens, the profile in the outer region is progressively flattened. This trend decreases as the end of transition is approached at around G* = 61 1. Measured mean temperature distributions for the same conditions as in Fig. 15 are plotted in Fig. 16a, in terms of nondimensional temperature + = ( t - ?,)/(to- t,) versus y , where t , to, and t , are the local fluid, (b)
(a1
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0.8 - 0.6
0.6
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0.4
0.2
0
0
2
6
4
8
10
77
Flci. 15. (a) Development of mean velocity profiles. (b) Variation of Urnax/iinlax during transition for experimental conditions of x=22 cm and p=8.36 atm (from Mahajan and Gebhart. 1979). Data: X , G* =434; 0 . 4 7 0 : 0.503; @, 543; 0,579; 0 . 6 1 1; 8, 648.
264
B . Gebhart and R . L. Mahajan
10
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Laminar theory
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surface, and ambient fluid temperatures, respectively. At G* = 470, the temperature profile is in agreement with the laminar profile. Note that at this value of G*, velocity transition had already begun. At G*=503, immediately downstream of the beginning of thermal transition at GFT= 480, the measured AT has already decreased from the laminar value (see Fig. 16b). The mean temperature profile has also started to deviate from the laminar trend. As thermal transition progresses, the thermal boundary layer thickens. The profiles steepen close to the wall and flatten in the outer region. These deviations follow those of velocity field, as expected, since they are initially almost completely coupled. As the flow penetrates into the ambient, it diffuses warm fluid outward, thereby thickening the thermal boundary layer, At the end of transition, at G* = 61 1, this modification is almost complete. Further variation with increasing G* is small. The mean velocity and temperature distribution modifications during transition in water show similar trends (see Jaluria and Gebhart, 1974). B. GROWTH OF THE BOUNDARY REGIONAND THE CORRELATION OF DISTRIBUTIONS DURING TRANSITION The increasing penetration of the upward flow into the ambient flow, with increasing transition, amounts to a more rapid growth in boundary region thickness. In air, the thermal and velocity boundary layers grow together. In water, the velocity boundary layer starts increasing in thickness
Buoyancy- Induced Flows
265
from its laminar value earlier due to delayed thermal transition. Although the thermal boundary-layer thickness grows more rapidly after the onset of transition, it does not catch up with the velocity region thickness either by the end of transition or even further downstream in fully turbulent flow. It is of interest to see if mean velocity (U/UmaX)and temperature (G) distributions can be correlated as a function of some dimensionless distance away from the wall. The laminar similarity variable q = y / 6 can not accomplish this (see Fig. 15a). When the temperature distribution in Fig. 16 is plotted in terms of 11, the same conclusion is indicated. Godaux and Gebhart (1974) showed that a modified q , defined as ,Y/&, or ,~/6,,, where aVMand ,a-, are, respectively, the measured local values of velocity and temperature boundary-layer thicknesses in transition is also not successful. Other attempts to correlate fully turbulent flows by a single variable, e.g., 77 = (y/x)Gr:' by Cheesewright (1968), have not been successful. For fully turbulent flows, however, George and Capp (1977) have recently shown that two different scaling parameters, one close to the wall and the other further out, correlate reasonably well the mean velocity and temperature distributions. Very near the wall there is a conduction viscous sublayer in which the mean temperature and velocity profiles are linear. In the other layer, called buoyant sublayer, the mean temperature and velocity profiles show, respectively, a cube root dependence and an inverse cube root dependence on distance from the wall. These predictions have found corroboration from the experimental work of Qureshi and Gebhart (1978). The data of Mahajan and Gebhart (1979) from the end of transition to early turbulence (in Fig. 16), when plotted in terms of these scaling parameters, also support these findings. However, examination of the data indicates that this scheme of scaling does not correlate distributions during transition. The two layers, inner and outer, are not clearly differentiated and the temperature in the outer layer decays faster than the indicated y ' I 3 . ~
C. DOWNSTREAM VELOCITY AND TEMPERATURE DISTRIBUTIONS
As the boundary layer undergoes transition, disturbances are found to amplify as they are convected downstream (see Fig. 17). The disturbance data of Mahajan and Gebhart (1979) in air, and of Jaluria and Gebhart (1974) in water, are plotted in the bottom part of Fig. 17 in terms of measured values of the maximum temperature and velocity fluctuation levels t' and u', respectively, normalized by the measured local mean-flow maximum values A t = 1,- t , and U,,,. Following the beginning of transition there is a rapid increase in disturbance magnitudes. The disturbances then grow less rapidly during later stages of transition. After reaching
B . Gebhart and R . L. Mahajan
POINT NO.
400
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600
800
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1400
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--.
velocity data: temperature FIG. 17. Downstreams growth of disturbance level. -, data. Data in water: A, Jaluria and Gebhart (1974); Bill and Gebhart (1979). Data in air are from Mahajan and Gebhart (1979) (for legend of their data see Fig. 15).
m,
maximum values the ratios tend to decrease as the end of transition is approached. In air, the velocity and temperature fluctuations reach their maximum almost simultaneously. In water, on the other hand, the velocity fluctuation ratio reaches its maximum by the end of transition, whereas the temperature fluctuation ratio continues to grow. This lag in growth characteristic is a continuation of the lag in the earlier stages of transition. Bill and Gebhart (1979) examined this point in detail, taking measurements in water during the later stages of transition and further on, to fully developed turbulence. Their data are also shown in Fig. 17, plotted as (?2)'/2/(f'2)',/,2, and (li'2)'/2/(Z'2),!,(~ versus G*. The data point 3 corresponds to the end of transition. Heat-transfer measurements suggest that points 1 and 2 are in fully developed turbulent flow. Thus, although transition ends at point 3,
Buoyancy-lnduced Flows
267
turbulent heat-transfer mechanisms are not fully developed until the maximum temperature fluctuation level is reached (point 2). The region between points 3 and 2 is the zone of rapid spectral change, defined earlier, in which the turbulent parameters adjust themselves from the end of transition to fully developed turbulent values.
D. PROFILES OF DISTURBANCE FLUCTUATIONS Distributions of temperature and velocity fluctuation levels across the boundary region, from laminar flow, through transition, to early turbulence, in air, are shown in Fig. 18. The disturbance data during transition
7l
(b)
FIG.18. Velocity (a) and temperature (b) disturbance distributions across the boundary region in air. -, theoretical curve for G* =4W,11*= 1.23. The data of Mahajan and data points in early Gebhart (1979) are during transition (for legend see Fig. 15). The turbulence from Smith (1972).
m,
B . Gebhart and R. L . Mahajan
268
from Mahajan (1977) are plotted in terms of instantaneous values, whereas the data of Smith (1972), in early turbulence, are expressed in terms of rms values. In laminar flow, the disturbance profiles are in good agreement with the calculated laminar curves of Mahajan (1977) computed from linear stability theory for two-dimensional disturbances. However, as transition progresses, the distributions extend further out, with the thickening of the boundary layer. They deviate progressively from the laminar calculations. In particular, the position of the inner peak moves closer to the wall while the peak in the outer region broadens and finally disappears with the development of turbulence. As the end of transition is approached, the disturbance profiles adjust themselves to a fully developed turbulent distribution. Compare the profile of Mahajan (1977) at the end of transition to that of Smith (1972) in early turbulence. Data of Jaluria and Gebhart (1974), in water, show similar trends except for a persistence of the outer peak in distributions of velocity fluctuations, even at the end of transition. However, the data of Bill and Gebhart (1979), in early stages of fully developed turbulent flow, based on rms values of the disturbance fluctuations, show no such peaks. Nor is such a peak expected, since the turbulent diffusion would tend to smooth out sharp gradients in the boundary layer. Noting that the distributions of Jaluria and Gebhart are based on the maximum values of the fluctuation, as seen in an analog
1.0
1
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Buoyancy-Induced Flows
269
record, it is quite possible, as pointed out by Bill and Gebhart, that the peaks observed might represent the passage of particular bursts of turbulence. Progressive penetration of disturbance fluctuations into the thickening boundary layer as the flow progresses from laminar to turbulent can also be expressed in terms of distributions of intermittency factors I , and I,. I, distributions during transition from the experiment of Mahajan and Gebhart (1979) in pressurized nitrogen are shown in Fig. 19. Corresponding I, distributions, although not shown, are identical and follow the same developments. In early stages of transition, the region of maximum turbulence is located around the inflection point and flow is not fully turbulent ( I , = 1) anywhere. However, as transition progresses, the intermittency rapidly increases and spreads in both directions from the inflection point. The process continues until, at some value of G*, both I, and I, distributions change little further downstream. This by definition is the end of transition. In water, although the temperature disturbance layer is smaller in thickness than the velocity layer (the Prandtl number effect), the data of Jaluria and Gebhart (1974) indicate that as the end of transition is approached, both I, and I, distributions reach their final shape almost simultaneously and thereafter change insignificantly further downstream.
E. DISTURBANCE FREQUENCY DURING TRANSITION The selective amplification or filtering effect predicted by linear stability analysis has been found not only in the earlier stages of laminar instability, where linear processes dominate, but also in the region of nonlinear and three-dimensional disturbances, as discussed in Section IV, B. It is of interest to see if this filtering mechanism is modified during transition. An analog record of naturally occurring disturbances during transition in water, taken from the experimental investigation of Qureshi and Gebhart (1978), is shown in Fig. 20. In locally laminar portions of the flow, the disturbance frequency remains essentially unaltered during different stages of transition. Further, this frequency is the same as the filtered frequency predicted by linear stability theory (see the data at large G* in Fig. 4). The data of other investigators had shown this same result (see also Fig. 3, for comparable data in air). The process of selective disturbance amplification seems to extend far beyond the range of linear development and downstream well into transition. In Fig. 20, it is seen that other and higher frequencies also arise, later in transition. These disturbances begin to occupy a larger part of the record, that is, extent of the flow field, at the expense of the characteristic frequency. The disturbances become distributed over a much broader
270
B . Gebhart and R. L . Mahajan
(el
(fl
FIG. 20. Analog record of amplification of natural oscillations as the laminar flow undergoes thermal transition. (a) G*=682, (b) 889, (c) 962, ( d ) 1155, (e) 1375, ( f ) 1561 (Qureshi and Gebhart, 1978).
frequency range. This is the beginning of the broad range of length scales or eddy sizes that characterizes the eventual completely turbulent flow. An experimental determination of this frequency broadening during transition, and after, is provided by the s p e c t r y analysis of Bill and Gebhart (1979) (see Fig. 21). Cumulative spectra J$+df for the disturbance energy ii’*are presented for the flows a t the beginning of transition, the end of transition, and in full turbulence. The cumulative spectrum covers only the frequency range 0.006-10 Hz, since above 10 Hz the low levels of the spectral density approached the noise levels of the anemometer unit. Arrows in Fig. 21 correspond to the characteristic frequencies of the local flow. Near the beginning of transition, only about 5% of the disturbance energy lies above the characteristic frequency. About 45% of the disturbance energy is concentrated in a smdl frequency range containing the characteristic frequency. By the end of transition turbulent energy has been extracted from the mean flow through nonlinear processes and distributed more evenly across the spectrum. Approximately 14% of the energy is now distributed in the frequency range above the filtered frequency. This value is somewhat conservative, since the energy spectrum was cut off at 10 Hz, although some energy may be contained in the range above 10 Hz. Broadening of the spectrum continues beyond the end of transition. For the data in turbulence, energy above the filtered frequency increases to about 27% of the total disturbance energy. Further downstream, the spectrum of turbulence continues to develop until a condition is reached in which regions of local isotropic turbulence exist at “inertial sub range.” (For further details, refer to Bill and Gebhart (1979).) It is apparent from
Buoyancy-Induced Flows
27 1
1.07
-
0.8
J
'$df 0.008
0.6
-
0.4
-
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-
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Frequency (Hz) FIG.21. Cumulative energy distribution versus frequency: 0. the beginning of transition: transition: W, in turbulence. Data are taken From Bill and Gebhart (1979).
0;end of
Fig. 21 that the process of breaking up of large-scale eddies into smaller scales begins during transition. Taking disturbance frequency as a measure of turbulent length scales, the length scales during the early stages of transition are large since the observed laminar filtered frequencies are very low. However, as transition progresses, energy is transferred from the narrow band of frequencies centered on the characteristic frequency, to higher frequencies that indicate smaller-scale eddies.
F. THERMAL TRANSPORT DURING TRANSITION The most important practical aspect of transition is the improvement in heat-transfer mechanisms, compared to steady laminar flow. The progression of local heat transfer according to the laminar mechanism apd after is shown in Fig. 22. These data are from the experiments of Qureshi and Gebhart (1978), taken in flow induced adjacent to a vertical uniform flux surface in water. Accompanying the increase seen in local coefficient of
B . Gebhart and R . L. Mahajan
212
4
0
'
lo3
to2
10
10"
I 0l4
I 0''
FIG.22. Variation of local heat transfer from laminar through transition to turbulence. Data from Qureshi and Gebhart (1978): 0 , q=583.80; 0,1323.75; 2326.4; 0,3714.45; 0,4488.60 W/rnZ.
a,
heat transfer, h,, is a corresponding decrease in local surface temperature from its laminar value. The deviation from the laminar trend, the Jj root variation shown at smaller Gr:Pr, increases with the progression of transition, for each of the five heat flux levels. Eventually a fully developed turbulent heat-transfer trend is established further downstream. Clearly, the additional turbulent transport modes account for this more effective transport. The two possible modes are turbulent convection of heat downstream, p C F n , and increased transport of heat from the inner wall region to the outer boundary layer, p C F n . The downstream development of these modes, from the later stages of transition to turbulent flow, is shown in Fig. 23. Clearly there is an increase in both, with the maximum occurring beyond the location of end of transition. The increase in mode p C ' n is at the expense of mean thermal transport. As the flow deviates from the laminar condition, the streamwise velocity component U decreases progressively from its laminar value (see Fig. 15b). Since this decrease takes place in the region of steep temperature gradients, near the waii, there is a reduction of mean thermal transport. Since the downstream convection of heat is the aggregate of the convection by the mean base flow, JZpC, Ut dy, and the turbulent convection downstream,
273
Buoyancy-Induced Flows
0.0
‘
600
1
800
I 1200
It
1000
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1400
I
1600
G*
POINT NO. 4
3
2
--
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u‘t’lu’t’max; FIG.23. Downstream growth of turbulent heat transport 0,
.,
_u’t‘/u’t’max
at 7-6; q ” = 1920 W/m*. Data are taken from Bill and Gebhart (1979); vertical line is the location of end of transition from Jaluria and Gebhart (1974).
J , P p C p n d y ,a decrease in the former with progression of transition is overcompensated by an increase of the latter. As the flow undergoes transition, it penetrates further into the ambient and diffuses warm fluid outward. This results in the observed increase of the second turbulent transport mode p C p a (see Fig. 23). This increase is seen to lag the streamwise turbulent convective transport. The lag is similar to the delay observed in the development of temperature fluctuations (see Fig. 17). This suggests that the development of the normal heat-transport mode is more closely coupled to the temperature fluctuation levels in the wall region. Beyond the end of transition, the increase in both transport modes continues, which is to be expected. It is now known that fully developed turbulent heat-transfer mechanisms set in further downstream. In the intervening region of spectral transition, these transport modes therefore increase to adjust to the fully turbulent values. Thus, the modification of the laminar heat-transfer rate starting at the beginning of transition continues beyond the completion of transition, through the spectra! region, until the turbulent value is achieved.
214
B . Gebhart and R . L. Mahajan
V1. Predictive Parameters for the Events of Transition Perhaps the most important aspect of instability and transition studies is the establishment of predictive parameters for the two ends of transition. Both tradition and the success of linear stability theory in correctly predicting the dependence of the growth rate of two-dimensional disturbances, solely on the basis of the local Grashof number, led earlier investigators to attempt to use the Grashof number as the correlator of the beginning of transition. However, an examination of data (for example, as collected in Tables I and 11, indicates that each end of transition occurs over a broad range of Grashof number. Some of the spread may be attributed to different criteria. However, it is important to remember that there is no strong reason to believe that the prediction of transition events should depend solely on a parameter whose primary importance first arises in laminar transport and in the linear theory of stability. Strong nonlinear interactions precede transition. There may be many other important considerations. Vliet and Liu (1969) concluded from their experimental study of turbulent natural convection boundary layers that Ra: alone did not correlate the beginning of transition. No other parameter was proposed. The first experimental study to investigate this particular matter was that of Godaux and Gebhart (1974), in a flow induced adjacent to a uniform flux vertical surface, in water. The beginning of thermal transition was judged by traverses with a thermocouple probe at various downstream locations x, at different surface heat flux levels q” for each location. The data unequivocally proved that the beginning of transition was not correlated by local Grashof number alone. An additional dependence on at least x or q” was indicated. It was found that thermal transition, defined by the change in mean temperature profile from its laminar shape, began at an approximately constant value of G * / x 3 / 5 c c ( q ” x ) ’ / 5 aQ(x>’I5;that is, transition began when the local thermal energy Q(x), convected in the boundary layer at a downstream location x, had reached a certain value. The measurements of the mean and disturbance quantities during transition also confirmed the failure of G* alone to correlate transition (see, for example, Fig. 24). The thermal intermittency factor Z, for each flow condition is listed in the figure. At x- 100 cm, for G* =948 the mean temperature distribution has just deviated from the laminar. However, at x=36.2cm, it has already changed considerably at a much lower value of G*= 625. A similar conclusion follows from an examination of the disturbance data (not shown in Fig. 24). An additional downstream parameter must arise.
OF TRANSITION TABLE 1. DATA FOR THE BEGINNING
Transition Fluid
Pr"
Water Water N,
6.7 6.25-6.81 0.71
Air
0.71
Water
6.7
Water
5.05-6.4
Air Air Water
0.71 0.71 11.0
Water
11.4 6.7
G
G*
580- 1030 749-950 380-610 400-645
504-802 563-802 855-960
x
P
(cm)
(atm)
36.2-100 43.3-78.6 13.2-33 13.2-33 91.5 580 466 65 38.1 - 121.9 38.1-121.9 28-79
Instrument used to detect transition
I
Thermocouple Thermocouple Hot wire 1-15.92 Thermocouple I Thermocouple Thermocouple I 1 Hot wire Thermocouple I Thermocouple I
1 1- 15.92
E
EIE,h
Transition criterion
16.8-21.6 18.6- 19.4 16.8-23 17.6-24 24 23 13.6' 15.2 22.2"
0.82-1.05 0.9 1-0.95 0.86-1.17 0.86-1.17 1.17 1.12 0.70 0.74 I .08
25 30 16.3 20.5 17.2
I .28 I .46 0.8 I .03 0.88
As proposed in Section V" As proposed in Section V' As proposed in Section V" As proposed in Section VK AS proposed in Section V" As proposed in Section V" Jump in the frequency of disturbance above laminar frequency' Deviation of wall temperature from its maximum value During transition' During transition' During transition'?' During transition"' Beginning of vortex formation"
20
0.98
First appearance of Tollmien Schlichting waves" First appearance of turbulent burst'' First appearance of turbulent burstr
Air
0.70
400
61
1
Hot wire Thermocouple Thermocouple Hot wire Flow visualization using dye Interferometer
Air
0.71
622
92
I
Interferometer
26.4
1.29
CO,
0.77
460-547 645-702 54 I 378 605
12.5 25 17 9 25
Interferometer
23.8-24.9 23.2-26.4 24.4 18.3 19
1.16-1.21 1.13-1.29 1.19 0.89 0.93
572 713
84 97 24 27.4 60
1
485 665 665
I I I I
4-9 4-9 5 10 11
Proposed values of E for beginning of transition velocity transition. 19.5: thermal transition. 20.5. Prandtl number of ambient medium. Best fit value. dAverage value. 'Godaux and Gebhart (1974). 'Qureshi and Gebhart (1978). cMahajan and Gebhart ( 1979). Warner and Arpaci (1968). 'Jaluria and Gebhart (1974). /Vliet and Liu (1969). 'Colak-Antic (1964). 'Cheesewright (1968). "' Lock and Trotter (1968). "Szewczyk (1962). "Eckert and Soehngen (1951). [ ' R e p i e r and Kaplan (1963). "
TABLE I1
DATAFOR Transition G* G
X
P
(cm)
(atm) 4.18-15.92
Fluid
Pf
N,
0.71 495-980
13.2-33
Water
6.7
61
870
ENDOF TRANSITION
Instrument used to detect transition Hot wire and thermocouple Hot wire and thermocouple
990 I140 1320
Air Water
a
0.72 6.2 6.4 6.4 5.05
83.8 100.7 121.9 845 115 1140 113 1195 80.7 60.5 1385 1615 53.6
1
THE
1 1
Prandtl number of ambient medium. Q E T = I 1.4 for end of transition. Best fit value.
’Proposed value of
Thermocouple Thermocouple
QET
QET/QkT
Reference
11.4‘
1 .o
Mahajan and Gebhart (1979)
10.94
0.96
Jaluria and Gebhart (1974)
10.62 10.84 11.75 11.89 10.18 12.67 16.96 18.73
0.93 0.95
tb
scz
a-
F: “L
a
i3.
1.03
1.04 0.89 1.11
1.49 1.64
Cheesewright (1968) Vliet and Liu (1969)
% a a-
e. a 3
Buoyancy-fnduced Flows
277
-
&\\
0
Lam inar theory
3
2
I
4
rl Symbol
x(cm)
G*
0 0
36.2 36.2 36.2
485 608 625
I
r(cm)
G*
I,(7=2.5)
+
100
X
100
0.05 0.6
0
loo
948 1031 1131
I,(?J-2.5) Symbol 0 0.18 0.68
0.9
These striking results of Godaux and Gebhart (1974) generated a much more detailed investigation of transition by Jaluria and Gebhart (1974), also in water. This study confirmed that neither the beginning nor the end of transition is a function of only the local Grashof number. A function of the plate heat flux q” or, equivalently, of the streamwise coordinate x must also arise. Using both thermocouples and hot wires, it was found that velocity transition preceded thermal transition and that each began at a
278
B . Gebhart and R . L . Mahajan
particular value of G * / x 2 l 5 . The mean flow and disturbance quantities during the progression of transition strongly confirmed the above additional dependence on x . The end of transition was found to be approximately correlated by G * / x ’ . ~ ~ . A. CORRELATING PARAMETER E FOR THE BEGINNING OF TRANSITION The quantity G * / x 2 l 5 has a direct physical significance. It is proportional to the fifth root of the boundary-layer kinetic energy flux e , defined by
or e / p v 3=(G * 5 / x 2 ) F ( P r ) ,
where F(Pr) is a nondimensional function that may be calculated from the laminar similarity solution. Nondimensionalization of e / p v 3 in terms of g and v results in 2/3
e;/’=[$($)
or
] =(-$)
i!;:, ( i’3)
2/15
G*F(Pr)
(6.2)
2/15
--
-
-
G*= E,
where g x 3 / v 2 is the unit Grashof number. Jaluria and Gebhart (1974) found that velocity transition, indicated by the presence of higherfrequency disturbance components, began at E = 13.6. Thermal transition occurred later, at E = 15.2. An implication of these results is that the kinetic energy flux of the mean flow is the energy available for disturbance growth and this, in turn, determines the onset of transition. To test the validity of E as a general correlator of the beginning of transition, Jaluria and Gebhart (1974) calculated the values of E from the transition data of other investigators in air and in water, which are summarized in Table 1 of their article. A 70% spread in E was found, over a range of Pr=0.7-11.85. This spread is clearly due, in part, to the use of different criteria to identify the beginning of transition. This effect was demonstrated from the detailed experiments of Qureshi and Gebhart (l978), in water. The most commonly used methods of specifying transition were reviewed. They were as follows: (i) the appearance of significant temperature fluctuations, (ii) the deviation of the mean temperature profile from the laminar trend,
Buoyancy-Induced Flows
279
*0003 2000
G*
1000
-
500
-
,001 100
6
,
,
I
1000
1
I
I
I
1
1
1
1
1
1
10,000
q" (W/m2)
FIG. 25. E as a correlator of different criteria of beginning of thermal transition. ( I ) E = 17.5. appearance of significant temperature fluctuations in boundary layer, f ' = 0.05. (11) E = 19.2. deviation of mean temperature profile from laminar trend. (111) E=22.7. maximum surface temperature. Data are taken from Qureshi and Gebhart (1978).
and (iii) the attainment of maximum surface temperature for a uniform heat flux condition, the equivalent of the minimum heat transfer condition. It was found that each of these events is correlated approximately by a different unique value of E. Values of E for each of these different transition criteria, over a range of heat flux levels, are determined in Fig. 25. Constant-E parameter loci correlate each event. The value of E thus determined for the beginning of thermal transition in water, as defined by the deviation of mean temperature profile from the laminar trend is 19.2. This criterion is the one used in the correlation next discussed. A more rigorous test of E as a correlator of beginning of transition is provided by the experiments of Mahajan and Gebhart (1979), in pressurized nitrogen. Recall that the factor ( ~ * / g ) ~was / ' ~ introduced in the definition of E for nondimensionalization only. However, this imposes a particular dependence of G* on v, at the beginning of transition [see (6.2)]. Since v is inversely dependent on density in gases, this dependence was tested in transition experiments by changing the pressure level of nitrogen from 1 to 15.92 atm.
280
B . Gebhart and R . L. Mahajan
Measurements taken at a fixed level of pressure confirmed the dependence of the beginning of transition on G * / x ~ / ~However, . at a given downstream location, the values of G* (both G$T and G&) at which transition began showed a systematic dependence on pressure given closely by G * a p 2 / l 5 .Recalling that, for an ideal gas, v a l/p, these data indicate that G* a v - ~ / ' ' This . is different from the dependence G* a K4/I5implied by the definition of E in (6.2). Based on these dependences of the transition value G* on x and Y , the following new correlating parameter QeT for the beginning of transition in gases was formulated:
Here q is the fifth root of nondimensional local heat flux to the boundary region flow. Fixed values of QsT=290 and 315 were found to characterize the beginning of velocity and thermal transition, respectively. When calculated in terms of parameter E, transition data in nitrogen gas of Mahajan and Gebhart (1979) (see Table I) indicate an average value of 20.5 for beginning of thermal transition. Since this is very close to the value E = 19.2 suggested for the beginning of thermal transition in water, it is of interest to see if a single value of E can, within reasonable accuracy, predict the beginning of transition in both liquids and gases. To determine this unique value, the values of E were calculated from the data of various investigators concerning the beginning of transition. The results are summarized in Table I. The downstream locations, where not stated in some of the studies, have been estimated as accurately as the descriptions of the experiments permitted. Data for an isothermal surface condition was reduced using the relation
G = G*[ (0.q4/ - +'(O)] ' I 5 , where +'(O) is a Pr-dependent constant that is given, for example, in Table 8.1 of Gebhart (1971). For some of the data entries in Table I, the transition criterion was different from that proposed in Section V, as enumerated in the last column. Considering first the condition for the beginning of thermal transition, the data in the first four entries in Table I correspond to the same criterion, the response of a thermocouple probe. From this data, an average value of E=20.5 is indicated. The maximum difference from this value is 17%. Since the data correspond to the wide ranges G or C* =400-1030, x = 13.2100 cm, and p = 1-15.92 atm, this deviation in E is not surprising. The resulting estimates of G b or GTT,obtained using this single value of E to detect the beginning of thermal transition in both gases and water, should
Buoyancy-Induced Flows be sufficiently accurate for engineering calculations. Thus, G&=20.5( ~ . x ’ / Y - ) 2/15 .
28 1
(6.5) On the other hand, the beginning of thermal transition, as defined by the downstream location where the wall temperature begins to decrease from a maximum value (Vliet and Liu, 1969), appears to begin at an average value of E2522.2. This is close to the value of E=22.7 found by Qureshi and Gebhart (1978) for the same criterion. The observations in which an interferometer detected the beginning of transition resulted in a number of substantially higher values of E . This discrepancy is thought to be due to the insensitivity of the interferometer to small and/or concentrated turbulence. This is analogous to the differences noted in data for transition in supersonic boundary layers between Schlieren measurements and thermocouple measurements, as noted by Schubauer and Klebanoff (1956). Bill and Gebhart (1975) reached the same conclusion concerning interferometry, from their study of transition in plane plumes. The lower values of E for two data points of Regnier and Kaplan (1963) could also be due in part to inaccurate resolution of interferometer output for the low values of AT for these experiments. Earlier transition is suggested by the lower values of E for the data of Eckert and Soehngen (1951). This is possibly due to the particular nature of their experiment. Very high disturbance levels were present and the flow was actually a transient cooling of a surface. From the interferometric data in Table I, a representative value of E to mark the first appearance of turbulent burst seems to be about 25. For the beginning of velocity transition, as marked by deviation of U,,, from its laminar value (see Section V), the value of E in gases from the data of Mahajan and Gebhart (1979) appears to center around an average value of 19.5. This corresponds to a value of x for the beginning of velocity transition (xVT)to be 5% upstream of that for the beginning of thermal . this criterion, no such precise information is available transition ( x ~ ) For in water. In the detailed transition experiments of Jaluria and Gebhart (1974), in water, a different criterion was used. This criterion was the presence of a higher-frequency component, superimposed on a single laminar filtered frequency, as the indication of the beginning of velocity transition. This was found to occur at a location G* about 12% upstream of the location of the beginning of thermal transition. The deviation of U,,, from its laminar trend occurs in between the locations of these two events. Thus, it is not unreasonable to assume that the beginning of velocity transition, according to the criterion used here, takes place in water also at about 5% upstream of xn. Indeed, examination of the data in Fig. 15 of Jaluria and Gebhart (1974) also suggests this assumption. Thus, it appears
B . Gebhart and R. L. Mahajan
282
that in both gases and water, velocity transition occurs about 5% upstream of thermal transition. Using the proposed value of Em= 20.5, this amounts to a value of EvT=19.5. In other words,
B. PREDICTIVE PARAMETER FOR THE END OF TRANSITION As for the beginning of transition, the recent investigations have conclusively shown that the end of transition is also not correlated by G* aIone. Additional dependence on x, q", and/or v must be considered. Jaluria and Gebhart, in the investigation of water, found that G*/x", where n--0.54, approximately correlated the end of transition. No nondimensional parameter was proposed. The more detailed study by Mahajan and Gebhart (1979), in pressurized nitrogen, indicated n-0.50 and an additional depen1000
-
7
-000 900
700 600
G~~ 500 400
i // 0
-
0/
O
-
- 20
- -d
r+
- 15 m-
- 10 Q~~
- 5
Buoyancy-Induced Ffows
283
dence of G* on v as G* av-’’’(see Fig. 26). Based on these results, the following correlating parameter was proposed:
(6.7 1 where Ra* is the Rayleigh number for a uniform flux surface condition. The value Q E T from these data in gases was found to be 11.4 (see Table 11). The Prandtl number dependence as Pr’/’ in the definition of QET above was included to account for any independent effect of Prandtl number on QET.
The data of other investigators for the end of transition in air and water, converted to QET form, are-also listed in Table TI. As for the beginning of transition, there is much scatter in the values of G& or GET. However, when converted to QET, the data seem to collapse around the value of Q E T = 1 1.4. For the transition data of Cheesewright (1968), in air, the value of QET is 11.89. Note that his data is for an isothermal surface and was converted to the form of Q E T using (6.4) with +(O) taken at the value estimated from the data at the end of transition. The average value of Q E T calculated from the data of Jaluria and Gebhart (1974), in water, is about 11, with the maximum difference from the suggested value of QET being only 7%. The QET values for the first two data points of Vliet and Liu (1969) in Table I1 are close to those predicted. For the last two entries, however, the Q E T values are much higher. The values of A t across the boundary layer for these two data points were much larger (15-22OC>, leading to the uncertainty in property evaluation. The above observations suggest that a given value of Q E T is a consistent indicator of the end of transition. The Pr dependence included in the definition seems to be adequate at least for the data in air and in water. Based on the value of Q E T = 11.4, the following relation may thus be used to determine the location for the end of transition, using local sensors, to a reasonable degree of accuracy both in water and gases: Ra* = 308( ~
x ~ / P ~ ) ’ / ~ .
(6.8)
VII. Plane Plume Instability and Transition Plume flows are very different from those adjacent to a surface. The surface damps disturbances. They are also very different in that the two mirror-image flows of a plume may freely interact in disturbance mechanisms across the midplane and even by fluid motion across the midplane.
284
B . Gebhart and R . L . Mahajan
FIG.27. Plumes perturbed with sinusoidal disturbances at several frequencies for air at atmospheric pressure: f=2.4 (a); 3.6 (b); 5.1 (c), 7.0 Hz(d). Q’=56.3 W/m, wire length= 15.5 cm, wire diarneter=0.013 cm (Pera and Gebhart, 1971).
As a result, free boundary flows are much less stable (in G ) than those
adjacent to surfaces. Also, disturbance mechanisms that are asymmetric, with respect to the midplane, are found to be much more unstable than those that are symmetric. The plane plume may be thought of as arising in a wake above a horizontal concentrated source of energy, like an electrically heated wire.
Buoyancy-Induced Flows
285
The flow results entirely from thermal buoyancy. A plane plume in air, subject to controlled disturbances of several frequencies, is seen in Fig. 27. The midplane temperature to decreases approximately as ( t o- t,)a x i.e., n = -0.6 in (3.28). The velocity increases as x0,*. The local flow parameter is again G in (3.29), as for the vertical surface. The plane plume flow is discussed in detail in Section IX. Two-dimensional disturbances were postulated by Pera and Gebhart (1971) as in (3.35) and (3.36). The stability equations in terms of and s are again (3.39) and (3.40). The coupled base-flow temperature and stream functions (+ and F) are found from (3.31)-(3.33). The remote boundary conditions in Q, and s are still the same43.41). The other three conditions admit the possibilities of disturbance motion at 17 = 0 and of disturbances being symmetric or nonsymmetric about 17 = 0. An extreme of nonsymmetry is complete asymmetry. The asymmetric mode was found to be less stable and neutral stability curves were determined. The result for Pr=0.7 is the neutral curve of Fig. 28. The first values of G for instability were found to be very low, an order of magnitude less than those shown in Figs. 3 and 4 for flows adjacent to surfaces. Haaland and Sparrow (1973) repeated the stability analysis, retaining two of the several terms excluded in the conventional approximations, as set forth in Section 111. Similar results are obtained. 'The question of the consistency of higher-order approximations in stability analysis for vertical buoyancy-induced flows is considered in Section IX. The paths that disturbances follow as they are convected along at constant frequency are also indicated in Fig. 28. The particular frequencies shown are those relevant to experiments in atmospheric air at a source strength Q'=56.3 W/m. These paths show a very different behavior than for vertical flows adjacent to surfaces (recall Fig. 2). Also, the base flow amplifies all frequencies below a certain limit. However, all frequencies are eventually stable. Of course, this doesn't happen in an actual plume. Other and nonlinear mechanisms intervene for some of the amplified frequencies. Experiments by Pera and Gebhart (1971) tested these stability predictions. A 15.3-cm-long horizontal wire of 0.0127-cm diameter was electrically heated in atmospheric air. The interferograms of Fig. 27 show the extent of the thermal boundary region. Since, for Pr = 0.7 the velocity and thermal boundary regions are of almost equal extent, the region shown is essentially the whole plume. Controlled disturbances were introduced with the vibrator shown near the plume source. Disturbances of lower frequency are very strongly amplified. These observations are in very good agreement with the predictions of Fig. 28. We may conclude that the predictions of instability are again in close agreement with experimental observations, although the extent of the comparison concerns only the ranges of frequency and of G in which disturbances amplify.
B . Gebhart and R . L. Mahajan
286
-
QOl-
1
I 1 l l l l
I
I
I
I
I
I
I
I
I
I
I
FIG. 28. Computed neutral stability curve (Pera and Gebhart, 1971). Constant frequency contours for air for Q'=56.3 W/m. Data of highest frequency velocity disturbances: 0, Q'=65.9 W / m ; M, Q'=65.9 W/m (turbulent flow); v , Q'=3.1 W/m. Data are taken from Bill and Gebhart (1975).
Buoyancy- Induced Flows
287
Some calculations of amplification rate - a i have been made and the values are very large compared to those found for flows adjacent to surfaces. The low levels of G for instability and the rapid amplification rates, both from theory and as found in experiment, suggested that other nonlinear effects must very quickly (in x ) become important in such flows. Since the calculated downstream range of instability is very short (in G), even the relatively high values of - a i that were calculated result in maximum values of A of less than about 2.0 for the disturbance frequencies that appear to be sufficient to disrupt such plumes. Thus, such plumes are relatively much less stable than vertical flows adjacent to surfaces. A considerable amount of study has been devoted to plume transport, beyond the simple initial laminar flow that is amenable to similarity analysis. Some of these studies relate to transition, as do the foregoing stability analyses. Forstrom and Sparrow (1967) generated flows sufficiently vigorous to disrupt the laminar patterns. Thermocouple measurements indicated turbulent bursts and their first appearance was taken as the beginning of transition. Characterizing the local vigor of the flow by a local Grashof number based on the heat input rate, these occurred at the flow Grashof number, GrQ,,I , of 5 X lo8, where Q’ is the line source strength per unit length. This Grashof number is defined by GrQ,, =g&x3Q’/pCpv3. (7.1) At the highest heating rate used, and at the most distant location downstream, turbulent bursts were observed with great frequency. Furthermore, under this condition, a time-averaged temperature profile showed a thickening of the flow region, with respect to laminar flow. Based on this observation, Forstrom and Sparrow concluded that full turbulence occurred at Gr,.-.=5x lo9. Only this single data point was measured in what was taken to be the turbulent region. No comparisons could be made with the temperature decay in x for turbulent plumes predicted by Zel’dovich (1937). Even though flow at the highest Grashof number was found to be primarily turbulent, the maximum centerline temperature of the plume still was found to follow the functional dependence on heat flux predicted by laminar theory. It is noted that temperature levels for laminar flow depend on Q‘4/5, whereas in turbulent flow (either plane or axisymmetric) the dependence is indicated to be at least approximately Q’2/3. The turbulent data taken by Rouse et al. (1952) and by Lee and Emmons (1961) are difficult to interpret as thermal buoyancy-induced line source plumes since in the former study the plume flow was generated by a row of gas burners and in the latter by burning liquid fuel in a channel burner. In both experiments the plume source was of appreciable size and introduced initial momentum flux, diffusing chemical species of different molecular ~
288
B . Gebhart and R . L. Mahajan
weight, initial disturbances, and nonuniformity of energy production rate. Results of Lee and Emmons are tabulated only in terms of fuel consumption rate per unit length of burner. Perhaps related to possible additional mechanisms arising in such measurements are observations by Miyabe and Katsuhara (1972). Another mode of instability was seen in spindle oil. Transverse sinusoidal oscillations were reported, i.e., across the span of the plume. An experiment by Bill and Gebhart (1975), in atmospheric air, studied transition as it related to instability and to eventual turbulence. Using fine thermocouple and hot-wire anemometer probes, along with an interferometer, disturbances and turbulence conditions were studied in a plane plume subject to naturally occurring disturbances. The measured disturbance frequencies were in accord with the predictions of linear stability theory. Increasing local Grashof numbers were obtained either by increasing the heat input or by moving the probes further downstream. Velocity disturbance signals were decomposed with a spectrum analyzer. Somewhat surprisingly, it was found that all frequency components of appreciable amplitude fell in the amplified region of the stability plane, even to the end of transition. This indicates that linear stability considerations are important even in regions of large disturbance amplitude. This same characteristic was found during transition in the flows generated adjacent to a vertical surface, as discussed in Section V. The plumes were visualized with a 20-cm aperture Mach-Zehnder interferometer. Thereby, the locations of the thermocouple and hot-wire probes were known, in relation to the general flow configuration. The region considered to have turbulent bursts by Forstrom and Sparrow was found to consist of a flow in which two-dimensional sinusoidal-like disturbances had reached large amplitudes and higher-frequency disturbances had begun to appear. These large disturbances were seen to disappear downstream and leave a well-ordered and completely laminar boundary region. With increasing local Grashof number such disturbances became more frequent and eventually the laminar boundary layer broke down completely. This corresponds to the condition for which Forstrom and Sparrow reported a thickening of the profile and concluded the presence of complete turbulence. However, upstream of this last condition, the maximum instantaneous midplane temperature was still accurately predicted by the laminar theory. Further downstream, the changing centerline temperature finally came to depend on turbulent field parameters. In these observations, above 25.4-cm-long electrically heated wire at different downstream locations and heat input levels, these events occurred at roughly the same values of the local Grashof number. Thus, the beginning and end of transition approximately correlated in terms of this parameter.
Buoyancy-Induced Flows
289
Some of the patterns established for transition adjacent to a vertical surface, Jaluria and Gebhart (1974), are paralleled by this data. Twodimensional disturbances were found to amplify selectively. At increasing amplitude, three-dimensional effects became apparent. However, a delayed thermal transition effect was not observed. This might be expected in air (Pr = 0.7) since velocity and temperature disturbances appear to grow together and remain coupled. After a period of intermittency the flow adjusts to turbulent parameters. In the experiment, plumes were generated in an enclosure, from horizontal electrically heated wires of length L=25.4, 15.5, 5.1, and 2.5 cm and values of L/dw=741. 445, 400, and 400, where d,,, is the wire diameter. These plume spans, along with different levels of energy input, resulted in downstream plume behavior that varied from that of a plane plume toward that of an axisymmetric one. A measure of the downstream (in x) transport in a concentrated source plume is the nature of the decay of the temperature field, due to entrainment. This is expressed in terms of the actual midplane or axis fluid temperature io(x) as i,,(x)- t , =d(x) analogous to (3.28) in the similarity solution for plane laminar plumes. Here, io(x) is the time-averaged value. Each of the two plumes, plane (P) or axisymmetric (A), may be either laminar (L) or turbulent (T). The four variations are written below in terms of a general variable T , where I=g(Pr) is an integral of +F’:
T=4JZ( fo- t,)( p C p I ) / Q ’ . LP: T = Gr,; TP: T a IGr;’l2, LA: T=K,,(Q/Gr,)”*,
(7.5)
TA: T a K,, Q ’’rGr;5/4.
(7.6)
The value of the Grashof number Gr, in (7.3) and (7.4) is based on to- t , resulting from Q’, as calculated for steady laminar boundary-layer flow. A similar procedure is used in (7.5) and (7.6), using Q’ to calculate i o - t , from laminar theory. Comparisons of actual data with these trends were used to infer downstream plume transport. Typical examples of such transport are seen in Fig. 29 at two heat input conditions and at differing locations downstream. In Fig. 30 are shown the time variations of midplane velocity and temperature, at three downstream locations, in a given plume. The records in (a) and (b) clearly indicate that the velocity and temperature disturbances are strongly coupled, as would be surmised from the interferograms.
290
B . Gebhart and R . L. Mahujan
FIG. 29. lnterferograms for L=25.4 cm. G=68.8 (a, b). 186.0 (c). and 228.0 (d) at arrow locations. which are .x=7.1 and 30.5 cm. respectively. Q ’ = 5 0 (a, b). 98.1 W/m ( c , d ) (from Bill and Gebhart, 1975).
In (a) the temperature disturbance frequencies were found to be 0.2 Hz or less. These large fluctuations resulted from the swaying of the plume perpendicular to its average midplane, as well as from oscillations along its span. Despite these disturbances, the plume appeared to remain primarily laminar. This would be expected from Fig. 29a, where the listed local value of G applies at the level of the arrow. In Fig. 29b the flow is apparently still laminar, despite the large spanwise distortion seen. With increasing Grashof number, small-amplitude, higher-frequency disturbances begin to appear (Fig. 30b.) These are superimposed on the higher-amplitude, low-frequency disturbances seen at lower Grashof number. Simultaneously, large unsteady and wavelike disturbances were visible in the interferometer (as seen in Fig. 29b immediately downstream of the arrow marking the local value G = 186. These very complicated occurrences are taken as the first signs of local turbulence and are defined as the beginning of transition. In the following transition region, the laminar flow was intermittently disturbed by the passage of disturbances, followed by relaminarization. Yet further downstream, disturbance frequency and amplitude increased. The end of transition was taken as the location in x at which a thickening of the mean-flow boundary layer and no relaminarization occurred. Beyond the end of transition, the thermocouple and hot-wire outputs were dominated by high-frequency components (as seen in Fig. 30c.) The
Buoyancy- Induced Flows
I cm
29 1
(C)
FIG.30. Time variation of hot wire and thermocouple outputs. respectively, at G=68.8 (a) and 160.3 (b) and thermocouple output at G=228 (c). ---,laminar theory: L=25.4 cm,
Q'=34.4 W/m; chart speed=] crn/sec (From Bill and Gebhart, 1975).
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B . Gebhart and R . L. Mahajan
turbulent condition shown in Fig. 29d is characterized by a thickened boundary layer and a chaotic temperature field. Conclusions were not based primarily on a statistical study of the disturbances that arose under various conditions. 7 he flow had been found to be alternately laminar and turbulent early in transition. This suggested characterizing the flow locally in terms of the maximum measured instantaneous local temperature tb<x). These temperature trends downstream were then compared with (7.2)-(7.6), to indicate the kind of transport the flow was approaching downstream. It had been noted from experimental measurements in laminar flows that the measured T is about 15% below (7.3) (see Brodowicz and Kierkus, 1966; Forstrom and Sparrow, 1967; Schorr and Gebhart, 1970). Lyakhov (1970) demonstrated that this arose from flow generated upstream of the flow-generating electrically heated wire. Such on-flow is not included in the boundary-layer formulation, which restricts the domain to x > 0 for Q' > 0. Therefore this effect on T will again show up in subsequent comparisons. However, in Fig. 31 is 'shown the very interesting consequence already seen during the downstream transition processes of several other kinds of
LP; ----, FIG. 31. T versus Gr, data for nonturbulent plane plumes, in air: --, experimental correction; 0 , Forstrom and Sparrow (1967); Brodowicz and Kierkus (1966); 0 , , X , Bill and Gebhart (1975).
+
+,
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0.01
\ 0.001I I 0’
I
1
1
1
1
I
I
I
I
1
I
108
rx FIG. 32. T versus Gr, data for turbulent plumes taken from Bill and Gebhart (1975). -, LP: ----, TP: ---, TA; experimental correction. 0. Q ‘ = 5 0 W/m; m. 63.3: A, 75: 0, 84.6; v,98.1.
----.
vertical flows; that is, laminar transport continues to penetrate often, completely unchanged, far downstream into the transition region. Figure 3 I shows that measured instantaneous temperature maxima during transition are in excellent agreement with corrected laminar theory. The extent of the transition region is indicated on the figure. The first comprehensive data comparison (shown in Fig. 32) is for a plume initially of 25.4-cm span, for a range of energy input. The LP, TP, TA, and “corrected” LP (15% low) downstream trends are shown. Maximum measured instantaneous midplane temperatures are shown for plumes generated by five different levels of Q‘. Only the first two measurements at the lowest Q’ are seen to be still in the transition region. All the others are in completely turbulent flow; that is, they diverge downward from the LP corrected trend. Only the variation of T may be shown for the TP and TA plume, since the constants of proportionality in (7.4) and (7.6) are not
1
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B . Gebhart and R . L . Mahajan
known in general. These curves were placed to best agree with the data. For the TP plume, T is only a function of Grashof number. However, in the axisymmetric flow, there is also a further dependence on Q ” / * . The turbulent region data does not correlate well with either theory alone. Immediately after the end of transition, at perhaps Gr,=3X lo’, it conforms most closely to TP plume behavior. Further downstream the slope of the data decreases further and then conforms most closely to the trend for a TA plume. However, the data does not show systematic Q‘ dependence. The theories for turbulent plumes have been derived for mean-flow values and neither their accuracy nor their applicability to temperature maxima are established. Similar measurements for L = 15.3 cm indicated that transition is complete after Gr, = 4 x 10’. However, a similar plot does not show the succession of later trends seen in Fig. 32. For L = 5.1 cm the deviation, likely the achievement of full turbulence, did not occur until about Gr, = 2 x 10’. Thereafter the TP plume trend was followed. Surprisingly, for L = 2.5 cm, first deviation appeared to occur at a decreased value, at Gr, = 1.5 X 10’. The other important aspect of such a transition is how the predictions of stability theory relate to actual disturbance growth and transition. For example, it is seen in Fig. 28 that the theory prediction is for disturbance amplification only below a certain cutoff frequency. Disturbance velocity spectra were determined down to 2.5 Hz during the above measurements. Comparison of spectra at different values of Gr, for a given plume indicated which disturbance components had been amplified. The resulting points, in p and G , are shown in Fig. 28. These data are for L=25.4 cm at Q’=65.9 and 3.1 W/m. The trend of the data with G indicates that disturbance energy is found at increasingly higher frequencies further downstream. We also see that all disturbances detected up to G = 194 have, with one exception, traversed the amplified region of the stability plane. This is almost to the end of transition, which was about at G = 208. Beyond the end of transition, energy is found in higher frequencies, clearly indicating the kind of nonlinear disturbance growth and propagation mechanisms found by Jaluria and Gebhart (1974) in flows adjacent to a vertical surface. The spread of observed frequencies for G < 208 does not indicate a narrow-band filtering process, but a one-sided process. The much higher frequencies beyond G = 208 represent the conversion of disturbance energy by turbulent processes. This is a broadenidk of the spectrum, through turbulence. Finally, these estimates of transition limits are compared with those of Forstrom and Sparrow (1967). For the beginning of transition, the values are GrQ,*= 1 1.2 X 10’ and 5.0 X lo’, respectively. This discrepancy may in
Buoyancy-Induced Flows
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part be due to the insensitivity of the integrated interferometer output to small local disturbances. For the end of transition, the value of Bill and Gebhart (1975) is Grq..=7.9x lo9, compared to a single data point at 5 X lo9. The criterion for this latter value was a thickened temperature profile. This does not define a precise point for the completion of transition, and, from the later data, it appears that such a local flow was still within the transition region. In summary, the above measurements indicated that, for both L = 25.4 and 15.3 cm sources, the beginning of transition was at Gr, =6.4X 10’. It ended at approximately the single value Gr, = 2.95 x lo8. The correlation of centerline temperature with laminar theory provided a strong and unequivocal standard for the determination of the end of transition. After the complete disruption of the boundary layer, the flow begins to adjust to turbulent parameters, and the laminar centerline temperature is no longer achieved. Nonlinear effects have become important and spread disturbance energy to frequencies above those of the initially amplified disturbances. Turbulence intensity and scale then begin to decrease.
VIII. Instability of Combined Buoyancy-Mode Flows Mass transfer occurring in a fluid also gives rise to a buoyancy force if the molecular concentration gradient causes density differences. If the concentration of the diffusing chemical species is sufficiently small, the equations governing the phenomenon are identical to those governing a thermally induced flow. A frequently occurring circumstance in our environment and in technological applications is the simultaneous transport of both thermal energy and of one or more chemical constituents. The occurrence of a second buoyancy-inducing transport process may be expected to cause major alterations of the stability characteristics of the resulting flow. There are very complex interactions between disturbances in velocity, temperature, and concentration. The additional complexity may arise from two separate aspects. One is the possibility of opposing buoyancy force components. Then, the chemical species transport layers may be of different spatial extent. The measure of this is the Lewis number, Le= Sc/Pr = K / D,where Sc = Y / D is the Schmidt number. This additional characteristic is similar to the role of the Prandtl number in expressing the relative extents of the velocity and thermal effects. These effects may be seen in Fig. 33, in which buoyancy force distributions-f?,. thermal; B,, chemical; and B = B,+ &-are sketched for Le< I for both aiding and opposing buoyancy force components. Although combined buoyancy-mode flows appear to be very compli-
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B . Gebhart and R. L. Mahajan
3t
b
Y
FIG.33. Aiding and opposing buoyancy force components E , and E,. For Sc > Pr, the variation of the local buoyancy force B = ET+ B, for lo> r, and BT > 0. Gr, = Grx,I + Grr,c.N=Grf.,,./Gr,,l. (a) Local buoyancy force variation B for ) & ( f o - t , ) I > I,&(C,CJ. (b) Local buoyancy for reversal for I &.(Co- C,I > I &( t o - t J . Ea++ C, where C = ( C - Cm)/(C0- Cm).
cated, a very fortunate characteristic arises in a large proportion of the combined buoyancy-mode flows in our environment and in technology. First, the chemical species diffusion-caused density differences are often very small. For example, ordinary humidity levels in air are only a few percent of the total density. The discharge of solvents and other agents from many surfacing materials is often accomplished at very low gas-phase concentrations. Even for seawater, the salinity level is only about 3.5%. Yet
Buoyancy - Induced Flows
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the buoyancy effect resulting from the species diffusion is comparable to thermal buoyancy for a wide range of processes and conditions that very commonly arise (see Gebhart and Pera, 1971). In one of the first investigations of the flow resulting from combined thermal and mass transport, by Somers (1956), the dual buoyancy force variables were employed in an integral analysis. Gill er al. (1965) assessed the effects of multiple and comparable concentration levels. Possible similarity solutions were examined by Lowell and Adams (1967) and numerical results were presented by Adams and Lowell (1968). Among numerous experimental studies, the results of Bottemanne (1972) show close agreement with calculations. In formulating the instability of such transport at low level concentration, the similar methodologies in Gebhart and Pera (1971) and in Bottemanne (1971) will be followed. With small concentration differences, the buoyancy force contribution B , may be calculated in terms of the concentration differences as €3, =p&( C- Cm).This is analogous to the Boussinesq approximation in B,, in that the density is assumed to vary linearly with concentration C , where BC-is the equivalent volumetric coefficient of expansion. Then B = B,+ B , = g d PT( t - t m) + PCC c - C d l . Since the gradients of concentration are also small, both the Soret and the Dufour diffusion effects are negligible in a convective circumstance. Then the equations governing thermal transport and chemical species diffusion are equally simple and of identical form, except that the parameter of the first is the Prandtl number, Pr= Y / K , and of the second is the Schmidt number, Sc= v / D , where D is the Fickian molecular diffusion coefficient . Another fortunate characteristic is that the species diffusion rate is, relatively, very small. In particular, when the mass diffusion rate is converted to an equivalent velocity of the medium at density p, this velocity is usually very small compared to the flow velocities generated by buoyancy (see Gebhart and Pera, 1971). The resulting equation for convection and Fickian diffusion of a specie of local concentration C ( x , y , T ) is
aT
+ u-ac + 0-ac = D V’C, ax
ay
where C satisfies the general boundary condition
c(x,m,7)-cm=o.
(8.2)
+
The base-flow and disturbance levels are related by C(x, y , T ) = F(x, y ) C’(x, y , 7). The additional buoyancy force associated with C’ and the boundary region base-flow and disturbance equations are written, using the
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B . Gebhart and R . L . Mahajan
three approximations set forth in Section 111, as follows:
into The transformations in (3.26)-(3.30) may again be used to cast boundary-layer similarity form, with the following additions and modifications: 6=(c-C,)/(co-C,)=(C-C,)/e(x), e ( x ) = N , x ” , (8.6) Gr, = PGr,. ,+ MGr,,
[ PP,(I,-
=( g x 3 / v 2 )
G- cm)].
tm) + M P ~ (
(8.7) N =Grx A = P,(ioGrx.I
t,)lP,(
co- Cm),
(8.8)
where P and M are convenient constants and N is positive for aiding effects and negative for opposed. The functions b ( x ) and c ( x ) in (3.29) remain the same, as do the energy equation (3.32) and the conditions (3.33). The transformation of (8.4) and of the base-flow force momentum balance, with the additional buoyancy force term in 6, yields the following equations:
C‘” + Sc[ ( n + 3) F c ’ - 4 n F ’ 6 ] = 0, F”’ + ( n + 3 )FF’ - (2n + 2) ++ + NC“= 0. FI2
(8.9) (8.10)
Here P is taken as 1.0 and M as 0, following the analysis of Boura and Gebhart (1976). Then Gr, again becomes simply as given in (3.30). The characteristic length and velocity are again defined as in (3.34). These equations coupled with energy equation (3.32) have been solved for air and water for various practical values of Schmidt number and for multiple buoyancy effects aiding (positive N ) and opposing (negative N ) (see Gebhart and Pera, 1971). The disturbance stream and temperature functions J/’ and t’ remain as defined in (3.35) and (3.36). The disturbance C’is similarly defined in terms of an amplitude function a ( q ) : ~ ( xy , 7 ) = (
Co-
c,)a(q)exp[ i ( d x - /%)I.
(8.1 1)
The equation for a(?) from (8.5) becomes identical in form to that for s(q), (3.40), namely, ( F ’ - P / a ) u - era=(a”- a2u)/iaSc G.
(8.12)
Buoyancy-Induced Flows
299
The previous disturbance force-momentum balance (3.23) must now be augmented with the added buoyancy force component due to C ’ , as seen in (8.3). The result is that the disturbance velocity equation (3.39) is the same, except that 3‘ is replaced by s’+ Nu‘. The additional boundary conditions, on a, are analogous to those on s given in (3.41) and (3.47) for an assigned surface condition at q = 0: a(oo)=O,
a(O)=Ka’(O)
(8.13)
The above formulation for the amplitude functions @, s, and a, in terms of parameters cu,, q,p, Pr, Sc, N and G, is of seventh order. This, combined with the much greater complexity that may arise in the base flow with opposed effects when Pr # Sc, makes calculations much more difficult. Nevertheless, calculations have been made for the surface conditions t (x, 0, T ) = t,=constant and C(x,0,7)= C,=constant. Therefore, n=O and the full equations and boundary conditions, where G is as defined in (8.7) but with P = 1 and M = 0, are as follows: ( F ’ - @ / a ) ( @ ”-a2@)- F’”@=(~’”-2a2~”+cw4@+s‘+ Na‘)/iaG. (8.14)
(F’-/3/a)s-cp’@=(s’’-a2s)/iaPrG,
( F ’ - / 3 / a ) a- c“@= (a” - a a ) / i a Sc G,
9(0)= cp’(0)- s(O)= a(0)= @( 00)’
@‘(OO)=S(W)
= a(00)=0.
(8.15) (8.16)
(8.17)
It is apparent from these relations that a = d if Pr = Sc. Then the only effect of mass diffusion is through the coefficient of its buoyancy force term ( I N ) s in (8.14). Opposing buoyancy effects mean only that N is negative and (1 + N ) is reduced. Should ( I f N ) be found to be negative, it is replaced by -(I N ) and the assumed positive direction of x is reversed. In any event, the proper stability plane is that which applies for thermally caused buoyancy above. However, the interpretation is now different. The coordinates previously generalized in terms of Grx., must now be interpreted in terms of Grx,,( 1 N). However, the interesting question here concerns what additional effects arise when Pr # Sc, that is, for Le # 1. Then the buoyancy force variation is different and buoyancy force reversal may arise across the boundary region. The result may be large effects on the velocity distribution, which is usually the prime determinant of instability characteristics. For the most common fluids, air and water, the Lewis number for ordinarily occurring diffusing chemical species is usually different from 1 .O. For air, Pr-0.7, Sc ranges from 0.22 for hydrogen gas to around 2.5 for a hydrocarbon vapor, and Le ranges from 0.3 1 to 3.6. For CO,, Sc = 0.94 and
+
+
+
B . Gebhart and R . L. Mahajan
300
0.I4 -
0.10-
P
-
0.06-
0.02I
100
I
1
200
150
1
250
G FIG. 34. Neutral curves for Pr-0.7 and Sc=0.94 (carbon dioxide in air) in terms of thermal Grashof number.
Le= 1.34. For water at around 20°C, Pr-7.0, and Sc and Le range from 152 and 22 for hydrogen gas to about 1700 and 240 for sugar, respectively. For salt, Sc = 840 and Le = 120. Extensive stability calcuIations have been made for Pr = 0.7 and Sc = 0.2, 0.94, and 2.0. The remaining parameter to define a stability plane is N in (8.8). This is the ratio of the units of thermally and mass transfer-caused buoyancy. Figure 34 shows the effect of N on neutral stability for Sc=O.94 in terms of p and G as defined in (3.38) and (8.7),with P = 1 and M = O . Neutral curves for Pr=0.7, Sc=0.94, and six values of N, from -0.8 to +0.5, are seen. Increasing mass transfer buoyancy upward, that is, N >0, strongly destabilizes the flow in terms of G. This is to be expected, since G is not a reliable measure of the actual total buoyancy force. However, each of these neutral curves strongly suggests the very sharp selective disturbance amplification first found in a purely thermally driven flow. It amounts to selectively amplifying only certain components of a more complicated naturally occurring disturbance. A more realistic plot of these effects is seen in Fig. 35. There the
Buoyancy-Induced Flows
30 1
t y
0.14
b.2
FIG. 35. Neutral curves for Pr=0.7 and Sc==0.94 (carbon dioxide in air) in terms of a combined Grashof number.
coordinates are P I , and G , , instead. These are based on (8.7) for P- M = 1 as follows: (8.18)
pI= p( 1 + N ) - 3/4.
(8.19)
These coordinates are much more appropriate since Le= 1.34. The small effect on stability in the N range from -0.2 to +0.2 agrees with the conclusions of Gebhart and Pera (1971). A single neutral curve would result for Pr=Sc, for all N, when GI is used. The small difference in Pr and Sc is first strongly felt for N = - 0.5 and very strongly at N = - 0.8. The effect for N = -0.8 is seen here as formally due to the singularity of the transformation of ,l3 into p, at N = 1.0. This singularity does not actually occur for Le # 1.O; that is, we should not take P = M for Lef I .O because the two transport processes have different spatial extents, and their simple sum does not properly represent the actual buoyancy effect, or whatever
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GI -,
FIG. 36. Downstream disturbance amplification for Sc=0.94 in terms of G , . ----,N = 0 . 5 ; N s O . 0 : ...., N = -0.5.
else is appropriate as their combined effect. We recall that for Le = 1.0 there is no flow for N = 1.0, no matter what values are assigned to P and M. The downstream [ G ( x ) ] amplification rates are given by - ai. The ratio of the amplitude of any particular sinusoidal disturbance component downstream, at G, to the amplitude it had on crossing the neutral curve, at G,, is given by (3.43), where 4A there for the flux condition is here replaced by 3 A for the uniform surface condition of n = O . This amplitude growth calculation is approximate to the extent that the form of the disturbance amplitude distributions across the boundary region changes downstream with G and is also subject to all other approximations already made. The above integration is performed in the p,, G, plane along paths of constant physical frequency f. This path is PIG ; l 3= constant. Contours of constant A downstream have been calculated for Pr=0.7, Sc =0.94, 2.0, and 0.2, and for several values of N for each value of Sc. The contours have been determined across the band of frequency that experiences most rapid amplification in each circumstance. Again the frequencies most rapidly amplified are not the earliest in G to be unstable; that is, the notion of a critical G was again found not to be important. The results for Sc=O.94 and N = 0 . 5 , 0 and -0.5 are shown in Fig. 36 in terms of G I . The contours of A again show the sharp downstream frequency filtering found for a purely thermally driven flow and since abundantly corroborated by experiment. With the combined buoyancy modes,
Buoyancy- induced Flows
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we see that disturbances are amplified less rapidly for increasing N, in terms of G I . N = 0.5 and N = - 0.5 appear to cause opposite effects of comparable amount. Increasing N appears to stabilize the flow and also to reduce the most highly amplified frequencies. However, the location of the filtered band seems largely independent of N. Such inferences are not purely quantitative, since P = M = 1 is still somewhat arbitrary, even for Pr = 0.7 and Sc = 0.94. However, these results for Sc = 0.94 do not amount to a demanding test of the effects of combined buoyancy modes on stability and disturbance growth mechanisms. The transport effects are only approximately included by the parameter (1 + N). Recall that for Le= 1.32 the boundary layers are of comparable extent. For Sc = 2 (Le= 2.9), the concentration boundary layer is relatively thin. Stability results for Sc = 2.0 and N = - 0.5, 0, and + 0.5 are seen in Fig. 37 in terms of G I ,The effects of N on stability are much greater. An opposing buoyancy effect destabilizes the flow and an aiding one stabilizes. These effects are large. The destabilization for negative N is consistent with that found for Sc=O.94. We note that for values of Sc>Pr the concentration boundary layer is always thinner than the thermal one. Some results are also available for Sc=O.2, at N=O and 0.2. The
+
0.10-
PI
-
0.06-
I
I
I
I
200
100
I
I
I
G,
-.
I
400
300
I
I
I
500
FIG.37. Downstream disturbance amplification for Sc=0.2, in terms of G , . ----.N = 0 . 5 ; N=0.0;
. . . . , A'=
-0.5.
B . Gebhart and R . L . Mahajan
304 0.121
0.08
I t
c
0.04
I
100
I
I
200
1
I
300
I
I
1
400
FIG.38. Downstream disturbance amplification for Sc =0.2, in terms of G, . ----,N = 0.2; -,
N = 0.0.
calculations were limited to the A =0, 0.5, 1, and 2 contours because of long computing times. They are shown in Fig. 38. The curves indicate that a positive N again stabilizes. These results indicate stabilization with increasing N for all three values of the Schmidt number. This is rather surprising since this range of Sc spans the condition of Le= 1; that is, the concentration gradient layer is both thinner and thicker than the thermal layer, over the range. The explanation for this is not now clear. There have been no experiments for comparison, even to the extent of measured favored frequencies. Nevertheless, these results might be expected to be realistic estimates of the stability characteristics of actual flows because of the detailed past successes of linear stability theory, compared to many experiments, in its predictions of disturbance growth rates, filtered frequency, etc. There is the remaining question of how one may most accurately estimate the effective local vigor of a flow induced by combined buoyancy modes. The effect of Lewis number on the respective spatial extents of the diffusion layers, and the differing resultant modification of the form of the velocity field, makes this a very complicated and still unanswered question. The methods used here may be directly applied to other important combined buoyancy-mode flows. Both bounded and unbounded flows of great practical importance arise through combined modes and in many different fluids.
Buoyancy- Induced Flows
305
IX. Higher-Order Effects in Linear Stability Analysis The instability characteristics of the different types of buoyancy-induced flows discussed in Sections 111, VII, and VIII were obtained using analysis based on parallel flow and conventional boundary-layer approximations. Using these approximations (see Section 111) Orr-Sommerfeld equations (3.39) and (3.40) were obtained from a complete set of stability equations (3.16)-(3.18) by omitting some terms of O(I / G ) from the latter eqwtions. These terms can be shown to involve derivatives of lower order than appear on the right-hand side of (3.39) and (3.40) and therefore may be neglected. For many flow circumstances of interest, this procedure is justified. For example, for a flow adjacent to a vertical surface, the location of the first instability occurs around G*-I00 (see Figs. 3 and 4), so that the error introduced due to neglecting terms of order O(I/G*) is small. Further downstream (higher G*), in the region of highly amplified disturbances the error is even smaller. This region is of interest, since it immediately precedes transition. However, for a plume generated by a line heat source, unstable conditions extend to very low values of G (see Pera and Gebhart, 1971). Using parallel-flow analysis, the lowest value of G, is calculated to be approximately 3. At such low values of G, it is to be suspected that effects arising from O(I / G ) terms neglected in the parallel-flow analysis may be nonnegligible. An improved stability analysis to better predict the instability characteristics of such flows and other flows in general at lower values of G must consider “nonparallel” and other associated effects in a consistent manner. Such effects have not been adequately investigated. Haaland and Sparrow (1973) considered this matter for a plane plume flow. In the analysis, the Orr-Sommerfeld equations were extended to include the effects of streamwise dependence of base-flow quantities. These terms are shown underlined in the following equations:
at.+,K+u’ar+,-+o‘-=K at) ai a7 ax ax ay ax
(9.2)
Equation (9.1) is the vorticity equation derived from Eqs. (3.15)-(3.17) linearized in disturbance quantities and by following the standard procedure to obtain the vorticity equation from the continuity and momentum equations. Here vorticity l=aG/ax - aii/ay and disturbance vorticity {’ = au‘/ax - au’/ay. Equation (9.2) is the energy equation derived from (3.18) linearized in disturbance quantities. It can be shown that these
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B . Gebhart and R . L. Mahajan
underlined terms are of O( 1 / G) and lower. However, as first pointed out by Hieber and Nash ( 1975), Haaland and Sparrow (1973) neglected other terms that are of the same order as those retained. There are higher boundary-layer effects of O( 1/ G) in the base flow. These, through interaction with the disturbance quantities, give rise to terms of the same order in the stability equations. Further, the terms arising from the x dependence in S' and from the x dependence of (Y for fixed physical frequency are also of O( 1 / C). An internally consistent higher-order stability analysis must also include all these terms. Such an analysis for the plane plume is given by Hieber and Nash (1 975). The higher-order boundary-layer plume solution is calculated and the stability of the resulting flow has been analyzed by a systematic expansion in the disturbance equations. This procedure and the results are outlined next. A. PLANEPLUMEFLOW
Using the asymptotic matching technique, higher-order boundary-layer effects were first calculated in terms of perturbation parameter E = Gr; 'I4, with the leading terms (zeroth order) satisfying the following governing equations: F0"'+ 1F F " - IF'F'+@,=O, 5 0 0 5 0 0 (9.3)
+," + $Pr( For& + F6+o) =0,
(9.4)
F{(O) = Fo(0)= 1 - +o(0)= F6( 00) = (Po( 00 ) = 0. (9.51 Note that these equations are exactly the same as (3.31)-(3.33) with n = - $ except that the coefficients of some of the terms in (9.3) and (9.4) are different. This difference is due to the different definitions of similarity variables used. In this work, q = ( y / f i ~ ) ( G r , ) 'whereas /~, Hieber and Nash use 1 = ( y / x ) ( G r X ) ' l One 4 . set of equations may be transformed into the other. The first-order equations in F , and ( P I were determined to be governed by F,"'+ 25 F0 F1" I5 F'F' 0 1 + I= 0, (9.6)
+
+
+
+
Pr( For$', + 2 F&,) $PrF;@,= 0, Fl(0)= 0 = F;'(O)=+',(O) a), F;( 00)' $ cot yFo(00).
(9.7) (9.8)
The zeroth-order plane plume solutions have been obtained by several investigators. Closed-form solutions for Pr = 2 and 2 were presented by Yih (1956), and later rediscovered by Brand and Lahey (1967). The most
Buoyancy-Induced Flows
307
comprehensive numerical solutions for a range of Pr = 0.01 - 100 were presented by Gebhart et al. (1970). The numerical solution to the first-order equations above is given by Hieber and Nash (1975). To assess the higher-order stability effects, more general forms of equations (3.35) and (3.36) were assumed: +b'(x,y , z) = 6U,@ exp[ i ( A ( x )-
/%)I,
('f x, y , t)= d ( x)s exp[ i ( A( x) -
where
A=
/&)I,
(9.9) (9.10)
S,'ac x ) dx.
As for the base flow, the disturbance quantities were also then expanded in terms of z, as @=@o(q)+E@l(q)+ * . . , s = So(?) ff
+ zsl(q) +
= &6= f f , +
Eff,
+
, ,
**.
(9.1 1 ) (9.12) (9.13) (9.14)
c=co+€cl+~~'.
where c=p/ff.
The linearized vorticity disturbance equation (9. I ) was then evaluated in terms of the higher-order base-flow and disturbance quantities defined above. Taking terms in different powers of E resulted in the following equations: ~ ~ : L ( @ o ) = FAi ~ o c,)(@; ( €'
- &Do)-
iaoFl'@o=O
:L(@,)=5,+ff,52
(9.15) (9.16)
(9.18) Here (9.19)
308
B . Gebhart and R . L. Mahajan
arises from the streamwise dependence of a. and the property that a. depends only upon P, being the eigenvalue of the inviscid problem. The leading term from the disturbance energy equation (9.2) is (9.20) so = %@o/ ( G - CO). At large distances from the plume, the disturbances vanish so that +(0 0 ) = 0.
(9.21)
The boundary condition at the center of the plume depends on the nature of disturbances, i.e., @(O) =0 For symmetric disturbances, (9.22) W(0) = 0 for asymmetric disturbances.
(9.23)
It was shown by Pera and Gebhart (197 1) that the asymmetric mode is less stable than the symmetric mode so that the appropriate boundary conditions are (9.21) and (9.23), i.e., @;(o)=o=@0(00),
(9.24)
0;(0)= 0 = 0 ( 00 ),
(9.25)
The equations (9.15) and (9.24) define the inviscid problem and can be easily solved to calculate a. and Q0 for a given value of P. To determine a , , first note that the homogeneous problem for is the same as that for !Do. It is therefore required that
(9.26) where x is a nontrivial solution of the adjoint homogeneous problem:
+
(FG - cO)(x”- (~lix) 2 F{x’= 0,
(9.27) x’(O)=O=x(00).
With a. and @, known, x is determined from (9.27) and t2 is evaluated from (9.18). To determine t , , @ ’; and at’’ are obtained by successive differentiation of (9.24); s’, is similarly derived from (9.20) and y is obtained from knowing a. at neighboring values of P, namely
F P
(Yo(
P + AP ) -
(Yo(
2 AP
P - AP ) .
,
(9.28)
aI is now obtained from (9.26), i.e.
(9.29)
Buoyancy-Induced Flows 0.14
r
309
--
=\
-*
1
40
80
I20
160
1
200
c 39. Constant-amplitude-ratio curves for plane plume flow. Pr=0.7. -, Hieber and Nash (1975): -.-..Haaland and Sparrow (1973); - x - x , Pera and Gebhart (1971). FIG.
Calculating the values of a. and a , for a range of fi, the neutral stability and amplification curves can be obtained. Using the series in (9.13), truncated to two terms, - a i = -(aOi+€ali), (9.30) where - a i is the desired amplification rate. In particular, for the neutral stability curve ( - ai= 0), l / ~ = G r - : / ~ G/2fi =
= -a,,/aOi.
(9.31)
As in Section 111, constant-amplitude curves can be obtained along paths of
constant physical frequency given by fJ;2/jG-1/3,
(9.32)
i.e., m = - f in (3.42). Figure 39 shows these curves for different values of A . They have been replotted here from the curves /3 versus G of Hieber and Nash (1975) in (52, G ) coordinates. Horizontal lines are again the constantphysical-frequency disturbance trajectories. For comparison, the neutral curve from parallel-flow results of Pera and Gebhart (197 1) is also shown. Clearly, higher-order effects have significant effect on the instability characteristics of plane plume flows. With the inclusion of these effects, the neutral curve exhibits both minimum Grashof number and a lower branch. Also shown in the Fig. 39 is the neutral stability curve obtained by nonparallel analysis of Haaland and Sparrow (1973). The apparent discrepancy in their results is due to the inconsistent approximations used in that analysis, as discussed before.
B . Gebhart and R . L. Mahajan
310
B. OTHERVERTICALFLOWS Higher-order stability effects for flows adjacent to a vertical flow have not been evaluated. An approach to solve the problem is outlined below. As for a plume, the analysis must include the terms contributed by the higher-order boundary-layer effects, along with those arising from streamwise dependence of both base-flow and disturbance quantities. First consider the higher-order boundary-layer effects. For an isothermal surface, these have been most recently analyzed by Hieber ( I 974), with perturbation parameter E =Gr; 'I4. Mahajan and Gebhart (1978) analyzed these effects for a uniform flux surface, c being equal to 5 / G * . To proceed with stability analysis, one first notes that, unlike in plume flow, there is a predominantly viscous inner layer next to the surface at q = 0, where the no-slip condition must be satisfied. Away from the surface in the outer layer, the viscous forces are negligible. For these two regions (inner and outer), two separate solutions (inner and outer) arise that must match in the region q = O ( l ) . These solutions may be obtained by the method of matched asymptotic expansions. Appropriate outer expansions for CP and s are for fixed q and r,+O,
@-a&)+ e,@?(q)+ €;@;(TI)+ s-sg(
q)
+
€,ST(
q)
+ +z"(
**.
11) + * ' *
,
.
(9.33) (9.34)
Appropriate inner expansions for fixed y and c,+O are
,
@.-YEl@;(q)+E;@1;(q)+ S-€,S;(q)+E:S;(q)+
where
-
0
.
.
(9.35) (9.36)
may be related to the base-flow perturbation parameter E , and is the inner variable. Also, as before, we introduce the following asymptotic expansions: E,
{=?/el
cr--cw,+Eiai+E:a2+ . . * ) c-c,+
E,Cl
+ EfCZ+
* * *
.
(9.37) (9.38)
Using these expansions in conjunction with (9.1), (9.2), (9.9), and (9.10), and collecting terms of like powers of c l , the governing equations for inner and outer vorticity (a:, CP;, . ..) and temperature disturbance (sg,s;, . . . ) functions can be obtained. These equations can then be solved for a0, a,,... for fixed values of p, from which the amplification curves can be obtained.
Buoyancy-Induced Flows LIST OF SYMBOLS a
A
E C C, D E
f R G GI
G*
Gr, Gr: h k
Le N N,
Nu,
P Pr 4,'
Q Ra Ra* P
sc I
T AT ii, L?
U V. W u'. c'. w'
Uc s y i
Species disturbance amplitude function. equation (8.1 I ) Disturbance amplitude. A = - fj:,,., dG Buoyancy force. see equation (3.5) Concentration Constant-pressure specific heat Species diffusion coefficient Transition parameter, E = G*( ~ ~ / g . x - ' ) ~ / ' ' Disturbance frequency Gravitational acceleration Modified Grashof number, 4(Gr,/4)'/4 G(I N)'I4 Modified flux Grashof number, 5(Gr;/5)'lq Local Grashof number. $,(lot,)x3/ju2 Local flux Grashof number. g/jTq"x4/kv' Heat-transfer coefficient Thermal conductivity Lewis number, K I D GrV,<./Gr,,,, see equation (8.8) Defined in equation (3.28) Local Nusselt number, h x / k Pressure Prandtl number p C p / k Heat flux Total heat Rayleigh number. Gr:Pr Flux Rayleigh number. Gr:Pr Temperature disturbance amplitude function. see equation (3.36) Schmidt number, v / D Temperature Absolute temperature t"-f, Components of base flow velocity in .r. .v directions. respectively Components of mean flow velocity in T . -v. z directions, respectively Components of velocity disturbance in x. .I>, i directions. respectively Characteristic base flow velocity Downstream distance Normal distance Transverse coordinate
+
Greek Symbols
6 Wave number 01
c;s
,8 Disturbance Frequency.
B m/u, fil p ( 1 + ~ ) - 3 / / 4
= 27rj
31 I
B. Gebhart and R . L. Mahajan
3 12 PT
A
s 6
9
0 K
x P Y
P 7
rc
@
dJ Q Q*
Volumetric coefficient of thermal expansion Species expansion coefficient Characteristic boundary-layer thickness Perturbation parameter v/s Transverse wavenumber Thermal diffusivity Wavelength Dynamic viscosity Kinematic viscosity Density Time Stream function Velocity disturbance amplitude function Nondimensionalized temperature excess, ( I - I ~ ) / to( I,) Generalized frequency. equation (3.42) Generalized frequency for uniform flux surface condition Subscripts
C ET n 0 r VT TT .r 00
Concentration End of transition Neutral Surface or midplane A reference level Beginning of velocity transition Beginning of thermal transition At x
In distant medium
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Bottemanne, F. A. (1972). Experimental results of pure and simultaneous heat and mass transfer by free convection about a vertical cylinder for Pr=0.7I and Sc=O.63. Appl. Sci. Rex 25. 373-382. Boura, A. and Gebhart. B. (1976). The stability of a vertical flow which arises from combined buoyancy modes A I C h E J . 22.94. Brand, R. S. and Lahey, F. J. (1967). Heated Laminar vertical jet. J . Fluid Mech. 14. 305-315. Brodowicz. K.. and Kierkus. W. T. ( 1966). Experimental investigation of laminar free convection in air above a horizontal wire with constant heat flux. Inr. J . Hear Mars Transfer 9. 81. Cheesewright. R. ( 1968). Turbulent natural convection from a vertical plane surface. J . Hear Transfer 90. 1-8. Colak-Antic. P. ( 1962). Dreidimensional lnstabilitatser - Scheinungen des laminar - turbulenten Umschhges bei freier Konvektion langs einer vertikalen geheizhen Platte. Sitrungsher. Heidelh. Akad. Wiss., Marh. - narurwisr. KI. p. 315. Colak-Antic. P. ( 1964). Hitzdrahtmessungen des Laminar-Turbulenten Umschags bei freier konvektion. Jahrh. WGLR p. 172. Dring, R. P., and Gebhart. B. (1968). A theoretical investigation of disturbance amplification in external laminar natural convection. J . Nuid Mech. 34. 551-564. Eckert, E. R. G.. and Soehngen. E. (1951). lnterferometric studies on the stability and transition to turbulence of a free-convection boundary layer. Pror. Gen. Disc. Hear Transfer. Meet. London: 1 1 i h - I 3 / h Sept., pp. 321-323. IME and ASME. Forstrom. R. J.. and Sparrow. E. M. (1967). Experiments on the buoyant plume above a heated horizontal wire. Int. J . Heat Mass Trunsjer 10. 321-331. Gebhart. B. (1971). "Heat Transfer." 2nd ed. McGraw-Hill. New York. Gebhart. B. ( 1973). Instability transition and turbulence in buoyancy induced flows. .4nn. Rev. Fluid Mech. 5. 213-246. Gebhart. B., and Mahajan. R. L. (1975). Characteristic disturbance frequency in vertical natural convection flow. Int. J. Hear Mass Transjer 18. 1143-1 148. Gebhart. B.. and Pera. L. (1971). The nature of vertical natural convection flows resulting from combined buoyancy effects of thermal and mass diffusion. Int. J . Hear Muss Transfer 14. 2025-2050. Gebhart. B., Pera. L., and Schorr. A. W. (1970). Steady laminar natural convection plumes above a horizontal line source. Int. J. Heur Mass Transfer 13. 161-171. George, W. K., Jr., and Capp. S. (1977). The natural turbulent boundary layer on a vertical flat plate. Winter A S M E Meet. Sess. 16. Gill. W. N.. Del Casal. E.. and Zeh. D. W. (1965). Binary diffusion and heat transfer in laminar free convection boundary layers on a vertical plane. Inr. J . Hear Mass Transjer 8. 1131-1151. Godaux. F.. and Gebhart, B. (1974). An experimental study of the transition of natural convection flow adjacent to a vertical surface. In!. J. Hear Mass Transfer 17, 93-107. Haaland. S. E.. and Sparrow, E. M.. (1973). Stability of buoyant boundary layers and plumes, taking account of non-parallelism of the base flows. J . Heat Transjer 95. 295-301. Hieber. C. A. (1974). Natural convection around a semi-infinite vertical plate: higher-order effects. Inr. J. Heat Mass Tran.$er 17, 785-791. Hieber. C. A., and Gebhart, 8. (1971a). Stability of vertical natural convection boundary layers: Some numerical solutions. J . Fluid Mech. 48. 625-648. Hieber. C. A., and Gebhart, B. (1971b). Stability of vertical natural convection boundary layers: Expansions at large Prandtl number. J . %id Mech. 49, Part 3. 577-591. Hieber, C. A., and Nash E. J. (1975). Natural convection above a line heat source: Higherorder effects and stability. Int. J . Heat Mass Transfer 18. 1473. Hocking. L. M.,Stewartson, K.. Stuart, J. T., and Brown. S. M.(1972). A non-linear instability burst in plane parallel flow. J . Fluid Mech. 51. 705-735.
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Jaluria. Y. (1976). On introduction of disturbances in a natural convection flow. Inr. J. Hear Mass TranSjer 19, 1057- 1063. Jaluria. Y., and Gebhart. B. (1973).An experimental study of non-linear disturbance behavior in natural convection. J. Fluid Mech. 61. 337-365. Jaluria. Y.. and Gebhart, B. (1974). On transition mechanisms in vertical natural convection flows. J. Fluid Mech. 66, 309. Jaluria, Y.. and Gebhart, B. (1977). On disturbance growth mechanisms in a buoyancy induced flow. Inr. J. Heat Ma.rs Transfer. 20. 434-437. Klebanoff, P. S.. Tidstrom, K. D.. and Sargent, L. M. (1962). The three dimensional nature of boundary layer instabilities. J. Fhid Mech. 12. I . Knowles. C. P., and Gebhart, B. (1968). The stability of the laminar natural convection boundary layer. J. Fluid Mech. 34, 657-686. Knowles, C. P., and Gebhart, B. (1969). An experimental investigation of the stability of laminar and natural convection boundary layers. Prog. Heat Mass Transfer 2. 99-124. Kurtz, E. F.. and Crandall. S. H. (1962). Computer aided analysis of hydrodynamic stability. J . Math. Phys. 41. 264. Lee, S. L.. and Emmons, H. W. (1961). A study of natural convection above a line fire. J. Fluid Mech. 11, 353-363. Lock. G. S. H., and Trotter. F. J. de B. (1968). Observations on the structure of a turbulent free convection boundary layer. fnr. J. Hear Mass Transj’er 11. 1225-1232. Lowell, R. L., and Adams, J. A. (1967). Similarity analysis for multicomponent, free convection. A I A A J. 5, 1360-1361. Lyakhov. Y. N . (1970). Experimental investigation of free convection above a heated horizontal wire. PMTF, Zh. Prikl. Mekh. Tekh. Fiz. No. I 1 [transl. in J. Appl. Mech. Tech. Phys. 1 1 , 3551. Mahajan. R. L. (1977). Higher order effects, stability and transition in vertical natural convection flows. Ph.D. Thesis. Cornell University. Ithaca, New York. Mahajan. R. L.. and Gebhart, 6. (1978). Higher order approximations to the natural convection flow over a uniform flux vertical surface. Int. J. Heat Mass Transfer 21, 549-556. Mahajan, R. L., and Gebhart, B. (1979). An experimental determination of transition limits in a vertical natural convection flow adjacent to a surface. J. Fluid Mech. 91, 131-154. Miyabe, K., and Katsuhara, T. (1972). Experimental investigation of the swaying plume above a heated horizontal cylinder. Mem. Kyushu Inst. Technol., Eng. 2, 9. Mollendorf, J. C., and Gebhart, B. (1973). An experimental and numerical study of the viscous stability of a round laminar vertical jet with and without thermal buoyancy for symmetric and asymmetric disturbances. J . Fluid Mech. 61, Part 2 , 367-399. Nachtsheim, P. R. (1963). Stability of free convection boundary-layer flows. NASA Tech. Note
D-2089. Ostrach, S. (1964). In “Theory of Laminar Flows” (F. K. Moore, ed.), p. 528 Princeton Univ. Press, Princeton, New Jersey. Pera, L., and Gebhart, B. (1971). On the stability of laminar plumes: Some numerical solutions and experiments. f n t . J . Heat Mass Transfer 14, 975-984. Pera. L.. and Gebhart, B. (1973). On the stability of natural convection boundary layer flow over horizontal and slightly inclined surfaces. Int. J . Heat Muss Transfer 16, 1147-1 163. Plapp, J. E. (1957). The analytic study of laminar boundary layer stability in free convection. J . Aeronaut. Sci. 24, 318. Polymeropoulos, C. E., and Gebhart, B. (1967). lncipient instability in free convection laminar boundary Layers. J . Fluid Mech. 30,225-239. Qureshi, Z. H., and Gebhart, B. (1978). Transition and transport in a buoyancy driven flow in water adjacent to a vertical uniform flux surface. Inr. J. Hear Muss Transfer 21, 1967-1979.
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Regnier. G. M.. and Kaplan, C. (1963). Visualization of natural convection on a plane wall and in a vertical gap by differential interferometry. Transitional and turbulent regimes. Proc. Hear Transfer Fluid Mech. Ins:. pp. 94- 110. Rouse, H.. Yih, C. S., and Humphreys. H. W. (1952). Gravitational convection from a boundary source. Tellus 4, 21. Schorr. A. W., and Gebhart. B. (1970). An experimental investigation of natural convection wakes above a line heat source. In(. J . Heat Mass Transfer 13. 557. Schubauer, G. B., and Klebanoff. P. A. (1956). Contributions on the mechanics of boundary layer transition. Natl. Advis. Comm. Aeronaut. Rep. 1289. Shaukatullah. H. (1974). Graduate School of Aerospace and Mechanical Engineering, Cornell University. Ithaca. New York (personal communications). Smith, R. R. (1972). Characteristics of turbulence in free convection flow past a vertical plate. Ph.D. Thesis. University of London, Queen Mary College. Somers. E. V. (1956). Theoretical considerations of combined thermal and mass transfer from a vertical flat plate. J. Appl. Mech. 23, 295-301. Stuart, J. T. (1965). Hydrodynamic stability. Appl. Mech. Rev. 18. 523. Szewczyk. A. A. (1962). Stability and transition of the free convection boundary layer along a vertical flat plate. Int. J. Hear Mass Transfer 5, 903-914. Tani, 1. (1969). Boundary layer transition. Rev. Fluid Mech. 1, 169. Vliet, G. C.. and Liu. C. K. (1969). An experimental study of turbulent natural convection boundary layers. J . Hear Transfer 91. 517-53 I . Warner, C. (1966). Turbulent natural convection in air along a vertical flat plate. Ph.D. Thesis, University of Michigan, Ann Arbor. Warner, C.. and Arpaci. V. S. (1968). An experimental investigation of turbulent natural convection in air at low pressure along a vertical heated plate. In!. J . Hear Mass Transfer 11. 397-406. Yih, C. S. (1956). Free convection due to boundary sources. Proc. Svmp. Use Models Geophy. Fluid Mech.. 1953, pp. 117-133. Zel’dovich, Y. B. (1937). Limiting laws of freely rising convection currents. Zh. Eksp. Teur. Fir. 7. 1463.
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Author Index Numbers in italic refer to the pages on which the complete references are listed.
A Adams, J. A., 297, 312, 314 Agranovich, Z. S.. 79, 22s Alber, I . E., 187, 189, 190, 191, 225 Alexander, L. G., 57, 63 Arpaci. V. S., 261, 275. 315 Atakan. S.. 42, 44, 65 Audunson, T., 247, 248, 249. 251. 252, 256, 258. 312
B Beal. S. K., 63 Benjamin. T. B., 87, 88, 90, 119. 122. 152, 181, 192. 215. 225 Benney, D. J., 75. 117, 182. 185.215.217, 225 Benny, J. D., 247, 312 Bill, R. G., Jr., 261, 266, 268, 270, 271, 273. 281. 286. 288, 290, 291, 292, 293, 295. 312 Bottemanne, F. A,, 297. 312, 313 Boura. A., 298, 313 Brand, R. S., 306, 313 Brenner, H., 2. 1 I , 63 Bretherton, F. P.. 222, 225 Brodowicz, K., 292, 313 Brown, S. M.. 247, 313 Burnside. W.. 214, 226
Chu, F Y.F.. 216, 229 Chu. V. H., 215, 226 Coantic, M.. 153, 161, 179, 221, 228 Cohen, B. 1.. 216, 226 Cokelet. E. D., 215, 226 Colak-Antic, P., 258, 259, 275, 313 Coldren, C. L., 57. 63 C o r m . S., 22. 63 Cousins. L B.. 57, 63 Crandall, S. H., 243, 314 Crawford, D. R.. 1 1 1 , 1S2, 169, 179, 187, 215. 218, 221, 222. 226 Cummins, H. Z., 31, 65 Cumo. M., 31, 40, 41. 63
D Dagan, G., 220, 226 Davey. A,. 75, 215, 217, 226 Davies. C. N., 63 Del Casal, E., 297, 3 / 3 DiGiovanni, P. R., 4, 25, 27, 28. 36. 59, 63 Dring. R. P., 236, 243, 313 Dukler, A. E., 63 Durgey, J. C., 221. 226 Durst, F., 42, 55, 56, 59, 60, 61, 63, 64 Dussan, E. B., 63
E C
Eckert, E. R. G., 235, 246, 275, 281, 313 Einav, S., 31, 32, 33, 34, 35, 36. 37. 38, 39, 40, 59, 63. 64 Emmons, H. W., 287, 314
Caponi, E. A,, 222, 226 Capp, S., 265, 313 Chan, W. K., 21, 59, 64 Cheesewright, R., 261. 265, 275, 276, 283, 313 Chen. B., 128, 129, 130, 137, 218, 219. 226 Chigier, N . A,, 42, 44,65 Chi,. H. H.. 63 Cho. S. K., 43, 64
F Farello. G. E., 31, 40, 41, 63 Farmer, W. M.. 41, 44,63 317
Author Index
318
Feir, J. E., 87, 88, 119, 122, 152, 181, 192. 215, 216, 225, 226 Ferguson, W. E., Jr., 90, 92, 103, 122. 214, 216, 217, 227, 229 Fermi, J. E., 90, 216, 226 Ferrari, G., 31, 40, 41, 63 Filonenko, N. N., 183, 229 Forstrom, R. J., 287, 292, 294, 313 Friedlander, S. K., 57, 63
G Garabedian, P. R., 129, 218, 226 Gardner, C. S., 77, 216, 226 Garstang, M., 153, 154, 178, 179, 221, 226 Gebhart. B., 233, 236,237. 242, 243. 244, 245, 246, 247, 248, 249, 251, 252, 254. 256, 258, 259, 261, 262,263, 264, 265, 266, 261, 268, 269, 270, 271, 212, 273, 214, 275, 216, 277, 278, 279. 280, 281, 282. 283, 284, 285, 288, 289, 290, 291, 292, 293, 294, 295, 297, 298, 301, 307, 308, 309, 310, 312, 313, 314, 315 George, W. K., Jr., 265, 313 Gill, W. N., 297, 313 Giovanangeli, 5. P., 153. 177, 179, 221. 228 Godaux, F., 246, 261,265, 274, 275. 277, 313 Goldsmith, H . L., 31, 64 Graham, R.,196, 229 Greene, J. M., 77, 196, 216, 226 Grose, P. L., 153, 154, 178, 179, 221, 226
H
Haaland, S. E., 237, 285, 305, 306, 309, 313 Hammack, J. L., 80, 226 Hasirnoto, H., 75, 90, 215, 226 Hasselrnann, D. E., 152, 220, 226 Hasselrnann, K., 90, 181, 182, 220, 221, 226, 22 7 Hayes, W. D., 215, 227 Hewitt, G. F., 51, 63 Hiefer, C. A,, 306, 307, 309, 310, 313 Hinze, J. O., 3, 4, 63 Hjelmfelt, A. T., Jr., 57, 6 3 Hocking, L. M., 247, 3 / 3 Holrnes, P., 196, 227 Huang, N. E., 153, 221, 227 Hui, W. H., 221, 226
Hurnphreys, H. W., 287, 315 Hutchinson, P., 63
J Jackson, E. A., 227 Jaluria, Y.,246, 247. 253, 254, 258, 259, 261, 262, 264, 265, 266, 268, 269, 213, 275, 276, 277, 278, 281, 283, 289, 294, 314 Johnstone, H. F., 57, 63 K Kaplan, C., 261, 275, 281, 315 Karnis, A.. 31, 64 Katsuhara, T., 288, 314 Keller, J. B., 10, 65 Khristoforov, G. N., 153, 178, 221, 229 Kierkus, W.T., 292, 313 Kinsman, B., 71, 227 Klebanoff, P. S., 250, 258, 281, 314, 315 Knowles, C . P., 244,245,246, 314 Kruskal, M. D., 77, 216, 226 Kuo, Y . Y., 153, 154, 221, 227, 228 Kurtz, E. F., 243, 314
1
Lahey, F. J., 306, 313 Lake, B. M.,15, 90, 122, 123, 152, 153, 154, 161, 169, 179, 214, 215, 216, 217, 221. 222, 226,227,229 Lamb, H., 71,214, 227 Lax, P., 216, 227 Lee, S. L., 12, 16, 17, 18, 19, 21, 25, 27, 28, 31. 32, 33, 34, 35, 36, 31, 38, 39, 40,42.43, 44,45, 46, 47, 48, 49, 50, 51, 52, 53, 54, 55, 56, 59,60, 61, 63, 64.65, 287,314 Levi-Civita, T., 215, 227 Lighthill, M. J., 68, 88, 215, 227 Lin, C. S., 64 Liska, J. J., 42, 64 Liu, C . K., 261, 272, 274, 275, 276, 281, 283, 31 5 Liu, J. T. C., 10, 64 Lock, G. S . H., 261, 275, 314 Longuet-Higgins, M. S., 120, 122, 125, 128, 146, 152, 183, 190, 215, 218, 219, 220, 221, 22 7
Author tndex Lowell, R. L.. 297. 312, 314 Luke, J. C., 71, 227 Lumley. J., 22, 63 Lyakhov. Y. N.. 292, 314
M Ma, Y.C., 146, 216, 219, 220. 222. 227 McLaughlin, D. W., 216, 229 McLean, J. W., 146. 183. 219. 220. 222, 227 Mahajan, R. L.. 244, 261, 262. 263. 264. 266. 267, 268. 269, 275, 276, 279, 280, 281, 282. 310. 313, 314 Malhotra, A,, 64 Marble. F. E., 4, 5, 8, 9, 10, 14, 64 Marchenko, V. A., 79, 225 Martin. D. U., 77. 100, 101. 102, 106, 146, 216, 217. 218, 219. 220, 222, 227 Mason, S. G., 31, 64 Masuda, A., 153, 154, 221, 227, 228 Mei, C. C.. 215, 226 Michell. J. H.. 215, 228 Miles. J. W.. 196, 228 Mitsuyasu, H.. 153, 154, 221. 227, 228 Miura, R. M., 77, 216, 226 Miyabe, K., 288, 314 Mockros. L. F., 57, 63 Mollendorf, J. C., 237, 314 Mollo-Christensen, E., 154. 216, 221. 228 Moulton, R. W., 64 Muller, P., 221, 227 Murray, J. D., 3, 4, 22, 23. 64
N Nachtsheim, P. R., 243, 314 Nash, E. J., 306. 307, 309, 313 Nekrasov, A. I.. 214, 228 Newell, A. C., 75. 215. 225
319
Otterman. B.. 12. 16, 17, 18, 19, 21. 35, 36, 59, 64
P Palazzi. G., 31. 40, 41. 63 Pasta, J., 90, 216, 226 Pera, L.. 237. 284, 285. 297, 298. 301, 307. 308, 309, 313, 314 Peregrine. D. H., 130. 132, 137, 146. 152, 218, 228 Phillips, 0. M., 116. 152, 220. 228 Pierson. W. J., 180. 228 Plant, W. J., 154. 221, 228 Plapp, J. E., 238, 243, 314 Polymeropoulos, C. E., 246. 314 Putman, G. L.. 64
Q Qureshi, 2. H.. 245, 261, 265, 269, 270. 271, 272.275, 278. 219, 281, 315
R Ramamonjiarisoa. A.. 153, 154, 161, 177, 179. 216, 221, 228 Rayleigh, Lord, 10. 64, 146, 215, 228 Regnier. G. M., 261. 275, 281, 315 Rikiishi. K., 153. 221, 228 Roskes. G.. 217. 225 Ross, D. B., 221, 227 Rouhiainen, P. O., 57, 60, 61. 64 Rouse, H., 287. 315 Rowlands, G., 216, 228 Rubenchik, A. M., 99, 217, 229 Rubin, G., II, 12, 65 Rubinow, S . I., 10, 65 Rungaldier, H., 90, 122, 214, 216, 227 Russell. J. S . , 214. 228 5
0
Ogden, D. M., 42, 64 Oikawa, M., 85, 228 Ono, H., 75. 90,215, 226 Ostrach, S., 242. 314
Saffman, P. G., 11, 58, 65, 77, 100, 101, 102, 111, 128, 129, 130, 137, 139, 143, 146, 152, 153, 169, 171, 179, 182, 185, 187, 189, 190. 191, 215. 217, 218, 219, 220, 221. 222, 225, 226, 227, 228 Sargent, L. M., 250, 258, 314
Author Index
320
Schorr. A. W.. 292. 307. 313, 315 Schuhauer, G. B.. 281, 315 Schwartz, L. W., 215, 228 Scott, A. C., 216. 229 Segur, H., 80, 226, 229 Sell, W., 221. 227 Shabat, A. B.. 71, 79. 80, 215, 229 Shaukatullah, H., 246, 315 Singleton. R. E.. 9. 15, 65 Smith. R . R., 261. 262, 267. 268, 315 Soehngen, E.. 235. 246. 275, 281, 313 Solov'yev, Y. P., 153, 178, 221, 229 Somers, E. V.. 297, 31s Soo, S. L., 3, 65 Sparrow, E. M., 237, 285,287,292, 294, 305, 306, 309, 313 Srinivasan, J., 42, 43, 44. 45, 46, 47, 48, 49. 50. 51, 52, 53, 54, 55, 64. 65 Stachiewicz. J. W., 57, 60, 61. 64 Stewartson, K., 2 15, 2 17, 226, 247, 313 Stock. D. E., 42, 64 Stokes. G. G.. 10, 65, 71, 73, 133. 146. 214. 229 Stuart, J. T., 247. 313, 315 Su, M. Y., 143, 145, 153.219, 220, 229 Szewczyk, A. A., 243, 258, 275, 315
T
Tam. C. K. W., 22, 65 Tani, I., 258, 315 Taylor, D. S . , 44, 65 Thomas, G. P., 130, 132. 137, 146, 152, 218, 228 Thyagaraja, A., 216, 229 Tidstrom, K. D., 250, 258, 314 Trotter, F. J. de B., 261, 275, 314 Tung, C. C., 153, 221, 227 U
Ulam, S., 90. 216, 226 Umhauer, H., 42, 6 3 Ungut, A., 42, 44,65
V Van Deemter, J. J., 3, 23, 65 Van der Laan. E. T.. 3. 23, 65 Vasiliev. 0. F.,3, 6 5 Vliet, G . C., 261, 272, 274. 275, 276, 281, 283, 31s von Zweck. 0. H.. 153, 178. 221, 229
W Warner, C., 261, 275. 315 Warsh. K. L., 153, 154, 178, 179, 221, 226 Watson, K. M., 216, 226 Webb, D. J., 221, 229 West, 8. J., 216, 226 Whitharn. G . B., 71, 72, 215. 229 Wigley. A., 42, 65 Wilton, J. R.,215, 229 Wright, J. W., 154, 221, 228
Y Yajima, N., 85, 228 Yarnada, T., 196, 229 Yefimov, V. V.. 153, 178, 221, 229 Yeh, Y., 31, 65 Yih, C. S.. 287, 306, 315 Yuen, H. C., 77, 90,92, 100, 101, 102, 103, 106, I I I, 122, 123, 130, 143, 146, 152, 153, 154, 161, 169, 171, 179, 187, 214, 216, 217, 218, 219. 220, 221, 222, 226, 227, 228, 229 Yule, A. J., 42, 44,6 5 "
Zakharov, V. E., 75, 77, 79, 80, 96, 99, I 1 I , 114, 124, 152, 181, 183, 196, 215, 217, 218, 220, 229 Zare, M., 42, 55, 63 Zeh, D. W.. 297, 313 Zel'dovich. Y. B.. 287, 315 Zuher, N., 22, 65
Subject Index A
base flow, 240-241 boundary conditions, 241, 245 Air buoyancy force components, 295-296 disturbance fluctuations, profiles. 267-268 characteristic frequency data, 246 downstream growth of disturbance levels, constant disturbance frequency propaga265-266 tion, 237 time-mean velocity. 56 developed turbulence, 259-273 velocity distribution, turbulent channel disturbance equations, 241 flow, 53 disturbances. downstream growth, 237-246 Anode current. laser-Doppler anemometry double longitudinal vortex system, 256 and. 3 1-32 governing equations, 241 hairpin eddies, 259-260 linear stability analysis, 305-3 10 longitudinal mean profiles, 257 B longitudinal rolls, 254-255 naturally occurring disturbances, 258-259, Band pass filtering process, 154- I55 269-270 Benjamin-Feir instability, 87-88 nonlinear disturbance growth. 247-259 Bifurcation, 128-146, 219 controlled experiments, 253-256 critical wave steepness, 131-132, 137-138 from naturally occurring disturbances, Stokes waves, 128-130, 133-136 258-259 three-dimensional, 133- 137 secondary mean motions, 247-253 wave pattern, 137, 139-145 role of, 257-258 wave profile, 129-130 streamlines, 248-252 Boundary-layer flow spanwise modification, 250-254 compressible laminar, 9-10 spectral development, 261-262 conservation equations, 12- 14 stability equations, 238-239 incompressible, 5-9 stability plane, 235-237, 244-245 continuity equation, 5-7 temperature distributions, 263-264 far-downstream region measurements. thermal transition, 262 33-37 transition mechanisms, 260-261 momentum equation, 6-7 transverse velocity disturbance, 247-248 particle migration. 2 1-22 two-dimensional velocity disturbance, Boussinesq approximation, 239, 296-297 247-248 Bretschneider spectra, 224-225 velocity transition, 262 calculated vs. experimental data, 176- 178 mean, 263-264 Buoyancy force, 239, 295-297 vertical flows, 310 Buoyancy-induced flows, 23 1-315, see also Buoyancy-mode flows, combined, 295-304 Buoyancy-mode flows; Plume flows; boundary conditions, 299 Thermally buoyant flows; Turbulence Boussinesq approximation, 296-297 approximation collection. 240-242 buoyancy force component, 295-297 32 I
Subject Index
322
chemical species diffusion rate, 297-298 transport, 295-296 concentration differences, 296-298 concentration, disturbance levels, 297-298 downstream disturbance amplification, 302-304 neutral curves, 300-301
C
Conservation equations laminar shear flows, 3-5, 12-14, 22-25 incompressible boundary-layer flow, 5-7 Coordinate perturbation solution, 7-9 far-out mixing region, 20 incompressible laminar shear flow, impulsive motion induced, 26-29 initial mixing region, 16- 19 Cross-wave perturbations, 98- 102
D
Dispersion relation calculated versus experimental data, 174, 179 deep-water gravity waves, 70 modulated wave train, 157-162 narrow-band homogeneous spectrum, 191, 194- 195 nonlinear wave fields, 153-180 perturbation frequency, 103 uniform wave train, 87 wave spectra, 163-172 weakly nonlinear wave train, 96 Doppler frequency shift, fluid velocity measurement and, 31-32 Double longitudinal vortex system, 256-258 Drag force, small-Reynolds-number flow, 22-23
Energy cumulative distribution versus frequency, 270-27 1 displacement, 196 disturbance, plume flows, 308 kinetic, flux, 278 leakage, 103, 106-110, 217-218 normalized modal, 93 Energy equation, wave train, 73 Envelope amplitude, 91 complex, nonlinear Schriidinger equation, 75. 77 time evolution, localized packets, 104- 105 uniform wave train, 86-87 Envelope correlation function, 189- 190 Envelope soliton, 77-86, 216 cross-wave perturbations, 98- 102 envelope curves, 85-86 even perturbations, 99, 101-102 frequencies, 102 instability growth rates, 102 number of, 85 oblique, 97 odd perturbations, 99- 100 properties, 79-80 wave pulses, 81-85 Envelope spectral function, 189-190 Euler equations, deep-water gravity waves, 69-71
F Fermi-Pasta-Ulam recurrence, 90-91, 103-105, 202, 216 Fluid velocity, 7-8, 21, 29 far-downstream region, 35 initial mixing region, 16-17 laser-Doppler anemometry, 30-33 particle-path-length discrimination scheme, 46-54 Force, particle, 6 Fredholm alternative, 137 Freon-12, droplet-size distribution, 40-41
E
Eddy motion, particle deposition diffusion mechanism, 56-58 dynamical response characteristic, 57-6 I Electric field, laser-Doppler anemometry and, 31
G
Gases, transition mechanisms, 261 Glass particle-air suspension, turbulent pipe flow, 54-56, 60-61
Subject Index Glass particle-water suspension, particlepath-length discrimination scheme, 46-48 Grashof num ber beginning of transition, 274 combined buoyancy-mode flows, 298, 300-301 downstream amplification. 302-304 end of transition, 274, 294-295 flux, 244 plume flows, 287-290 nonturbulent, 292-293 turbulent, 293-294 Gravity waves, deep-water, 67-229 calculated versus ocean and laboratory data. 177-179 discretized systems, 222-223 dispersion relation, 70 envelope soliton, see Envelope soliton frequency, 70-71 governing equations, 69-72 interaction coefficients. 223-224 large-amplitude effects, I 11-153 ocean; statistical model, 180-181 phase speeds, 22 1-222 Stokes waves, 7 I wave train, see Wave train Zakharov's integral equation, I 11-1 16
H Hairpin eddies, 259-260 Hasselmann's equation, 186 Heat-transfer mechanisms, during transition, 27 1-273
323
Laminar shear flow, 3- 10 conservation equations, 3-5, 12-14 considering drag and lift forces, 10-22 considering drag and lift forces, density effects, 22-30 considering Stokes drag, 3-10 incompressible, impulsive motion induced, 25-30 long-time solution, 29-30 short-time solution, 26-29 wall friction, 30 laser-Doppler anemometry technique, 30-40 lift force, 10-12 theories, 10-22 Laser-Doppler anemometry technique, laminar shear flow, 30-40 far-downstream region, 33-37 near-leading edge region, 37-40 operational block diagram, 32-33 optical gating, 42-43 optical measuring volume, 45-46 particle sizing, 41 -44 moderately small particles, 44-46 reference-beam, 43-44, see also Particlepath-length discrimination scheme optical arrangement, 49 turbulent shear flows, 40-56 velocity measurement, 30-33 Lewis number, 295, 299-300 Lift force, laminar shear flow, 10-12 drag and, 10-22 drag, density effects and, 22-30 Lorentzian spectra, 224-225
M 1
Impulsive motion, incompressible flow induction, 10. 25-30 long-time solution, 29-30 short-time solution, 26-29 wall friction, 30
Modulation-demodulation cycles, 90 Momentum equation, boundary-layer flows, 6-7 Move photography, high-speed flow visualization, 4 - 4 1 Moving fringe pattern scheme, turbulent pipe flow, 54-56, 60-61
L
N
Laminar mixing shear flow, 14-21 far-out mixing region, 19-20 initial region, 15-19
Nitrogen beginning of transition, 279-280 end of transition, 282-283
324
Subject Index
velocity intermittency distributions, 267268 velocity measurements, 263
0
Ocean waves, statistical model, 180-181 Optical gating, laser-Doppler anemometry, 42-43 Orr-Sommerfeld equations, 243, 305
P Particle concentration profiles, 36-37, 40 thickness of particle-free layer, 39 cutoff frequency, 59 density initial mixing region, 19 ratio, 7, 9 deposition, theories eddy diffusion mechanism. 56-58 eddy motion. dynamical response characteristics, 57-61 turbulent channel flow, 56-61 Doppler signal, 45-46 fractional volume 28 migration, 14-21 far-out mixing region, 19-20 incompressible laminar boundary-layer flow, 21-22 initial mixing region. 15-19 number density distribution turbulent jet, 50 turbulent shear flow, 48 number density-size distribution, 44-46 number flux-size distribution, 44 size distribution particle-path-length discrimination scheme, 46-54 turbulent shear flow. 47-48 sizing, laser-Doppler anemometry, 41-46 stream function, initial mixing region, 17-18 transport flow regime, turbulent pipe flow,
60 velocity, 7-8, 27 far-downstream region, 35-36
initial mixing region, 17- I8 near-leading-edge region, 38 velocity distribution particle-path-length discrimination scheme, 46-54 turbulent shear flow, 47 velocity-size distribution, 44-46 Particle-path-length discrimination scheme, 46-55 turbulent channel flow, 49-54 with wall film, 52-55 turbulent jet, 48-50 turbulent shear flows, 46-48 Plume flows, 283-295 boundary conditions, 308 constant-amplitude-ratio curves, 309 disturbance energy equation, 308 downstream transport, 289-290 governing equations, 306 Grashof number nonturbulent, 292-293 turbulent plumes, 293-294 instability, 284-288 interferograms, 284, 290 linear stability analysis, 306-309 midplane temperature, 289-29 I midplane velocity. 289-291 neutral stability curve, 285-286 sinusoidal disturbances, 284-285 transition, 288-295 Power spectrum, 180-181 Prandtl number, 299-300 beginning of transition, 274 end of transition. 275
R Relaxation distance, laminar shear flow, 4-5 Rayleigh problem, 10 Restabilization, 119-120, 125-128, 218 Reynolds number laminar shear flow, far-downstream region, 35 slip, 1 1 S
Saffman lift force, I I Schmidt number, 299-300 downstream disturbance amplification, 302-304
Subject Index Schrodinger equation, nonlinear, 74-76, 215-21 8 approximation, time evolution, 207-209 steady solutions, 76-77, 97-98 three-dimensional, % Shear flows, two-phase suspension. 1-65, see also specific flows boundary-layer flow, 9 interaction forces, 4 particle forces, 6 relaxation distance, 4-5 relaxation time, 4 Reynolds number, 1 I Sideband instability, uniform wave train, 88 Skin-friction coefficient. 30 Slip, Reynolds number, I I Solitary wave solution. 77 Spanwise modification alternating buoyancy-induced flows, 250-252 downstream, 253-254 Spectral aspect ratio, 171-174 Spectral correlation function, 181- 187 Spin slip, Reynolds number, 1 I Stability equations, 238-239 Stokes drag force, I 1 Stokes expansion, 214-215 Stokes waves. 71 bifurcated, 128-130, 133-136 Surface elevation dispersion relation, 70 Stokes waves, 71 T
Temperature distributions, 263-264 versus Grashof number, 292-294 Thermal capacity parameter, 245 Thermal transition, see Transition, thermal Thermally buoyant flows, initial instability, 234-237 Tollmien-Schlichting wave, 235-236 Transition beginning, 275 correlating parameter E . 278-282 criteria for identification, 278-279 disturbance frequency, 269-27 1 downstream sequence, 260-261 end, 276 predictive parameter, 282-283
325
mechanisms, 260-261 mean temperature distribution, 263-264, 274-277 mean velocity distributions, 263-264 plume flows, 288-295 predictive parameters, 274-283 thermal, 262 criteria of beginning, 279-280 transport. 27 1-273 velocity. 262 criteria of beginning, 281-282 Turbulence, buoyancy-induced flows, 259- 273 boundary region growth, 264-265 velocity intermittency distributions, 268-269 correlation of distributions, 264-265 disturbance fluctuations, profiles. 267-269 disturbance frequency, transition, 269-27 I downstream transition sequence, 260-261 downstream temperature distributions, 265-267 downstream velocity distributions, 265267 naturally occurring disturbances, 269-270 transition, thermal transport, 271 -273 Turbulent channel flow particle deposition theories, 56-61 eddy motion, dynamical response characteristics, 57-61 particle-path-length discrimination scheme, 49-54 with wall film, 52-55 Turbulent core, particle deposition theory, 56-58 Turbulent jet, particle-path-length discrimination scheme, 48-50 Turbulent pipe flow moving fringe pattern scheme, 54-56, 60-6 I particle transport flow regime, 60 Turbulent shear flows high-speed movie photography, 40-41 laser-Doppler anemometry, 40-56 particle-path-length discrimination scheme, 46-48
V Velocity, see also Fluid velocity; Particle, velocity
326
Subject Index
potential dispersion relation, 70 Stokes waves, 71 single-phase flow, 34-35 surface potential, 1 1 1-1 12 transition, see Transition, velocity Vertical flows, linear stability analysis, 310 Viscosity, fluid kinematic, 7 Vorticity equation, 305-307
W Wave conservation equation, 73 Wave field, nonlinear, 153-214. see also Wave train; Wave spectra band pass filtering process, 154- I55 behavior types, 174, 179- 180 discretized Zakharov equation, properties, 195-214 dispersion relation, calculated versus experimental data, 174, 179 dynamical systems, 196-209 homogeneous spectrum, stability to inhomogeneous disturbances, 187- 188 instability growth rate, 192 narrow-band, 188-190 homogeneous spectrum, stability to inhomogeneous perturbations, 190195 phase velocity, 155 random, spectral correlation function, I8 I - I87 stability, homogeneous, 192- 195 statistical properties, 180- 195 Wavenumber normalized perturbation, 119 spectrum. I80 Wave patterns, 219 bifurcated waves, 137, 139-145 Wave pulses evolution, 81, 84 head-on collision, 82, 84 overtaking and passing, 83-85 Wave spectra calculated versus experimental data, 175-178 dispersion properties varying bandwidth, 169- 172 varying nonlinearity, 163-169
dispersion relation, 163-172 narrow-band, 188-190 phase speed, 163-173 Wave train Benjamin-Feir instability, 87-88 concept, 71-73 free surface boundary conditions, 112 governing equations, 72 instability growth rate, 150-151 instability region, 147-150 Class I and 11, 151-152, 220 modulated calculated versus experimental data, 174- I75 phase speed, 157-162 properties, 157- 162 perturbed, 87 perturbation frequency, 120-121, 123 restabilization, 119-120 stability boundary, 128 curves, 128 growth rates, 126-127 steepness, 220-221 bifurcation and, 137-138 three-dimensional instability, 146- 153 uniform dispersion relation, 87 disturbances, 103 envelope, 86-87 initial condition, 209-21 I instability growth rates, 94, 106- 107, 119. 121-122 modulational instability, 86-89 nonlinear instability, 204-206 sideband instability, 88 stability, 117- 125 stability boundary, 106, 108, 124 stability diagram, 120, 202-204 three-dimensional modulation, 123- 125 time evolution, 212-214 two-dimensional modulation, 118-123 unstable, time evolution, 95, 106, 109-1 10, 197-202, 205-206 complex, 92-94 long-time, 89-90 long-time and initial condition, 90-96 simple, 91 weakly nonlinear, 72-96 energy leakage, 103, 106-1 10 perturbation frequency, 103
327
Subject Index properties, 96- 1 1 I quasi-recurrence, 103, 106-1 10 Schrodinger equation, 74-77 Water downstream growth of disturbance level, 265-266 downstream transition sequence, 260-261 naturally occurring disturbances. 269-270 Water droplet-air suspension migration, turbulent channel flow, 54 number density distribution, turbulent channel flow, 51 size distribution turbulent channel flow, 51 turbulent jet, 50
velocity distribution, turbulent channel flow, 52 Water-wave equations, solutions, 146
2 Zakharov integral equation, 218-219, 221 bifurcated waves, 130- 132 three-dimensional, 132- I37 derivation, I I I - I 16 discretized, 195-2 I4 nonlinear dynamical systems, 196-209 dispersion relation, nonlinear wave field, 154-155
stability boundary, 124
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