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Boundary Lyer Theory

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244 XI. Axially symmrtrical nnd tl~rcc-dirnertsionnl boundary lnyers<br />

Fig. 11.10. Ihg coefficirntr,<br />

oi n rotnt.ing spl~crr in axinl<br />

flow in trww of tl~c ltcJrnolds<br />

number R and rotntion<br />

Imramrtrr .Q - ioR/lI,<br />

h t.l~corct.iwl cxpl;~nntiou of t,hc vrry cwnplcx thrrc-dimrnsionnl cll'ccb in the boundary<br />

Iayrrof rotating I~odics of rcvolut.ion in axid flow is contained in the papers by H. Schlichting [00],<br />

IC. 'I'rnckrnhrotll~ [I181 antl 0. I'arr 1841; thcse authors onployed the approximato method<br />

!:xplainod earlior. It is t.rne that the boundary layer of a rotating body of revolution<br />

In axial flow still rctains it^ axial syn~mctry, hnt owing to the rotation there appears a peripheral<br />

vc1ocit.y cotnponent in addition to that in the mcridional direction. For this reason, the calculation<br />

for such a I)o~lntlsr,y layor must int,roduce a ~norncntom eqnat.ion in the circumferential direction<br />

(11-direr:t,ion) in atlclit.ion Lo that in tho n~crirlional direction (x-direction). Assuming that the<br />

a~~gulnr vclocit,y of t.11~ I~ody is io, antl ilcnoting t,he coordinate at right angles to the wall by y,<br />

wr ran writ.(: 1.11~ 1.~0 erluat.ions of n~otn~nl~un~ in tho form<br />

r.<br />

I hr component,^ or the shearing stress at thc wall are then given by<br />

~ig. 11.11. Position of line of laminar<br />

separation on a spl~ero rotating in axinl<br />

stream, after N. IF. Hosltin [SO]<br />

c. Iblation hel:ween axially ~y~ntnetrical and t\\o-cli~~~c~~aio~~;rl I,onntl;rry I;ryr~s 245<br />

and tho displacement and momentum thicknesses arc defined as<br />

m m<br />

In the procctling equations, the local pcriphernl velocity w, - r u) hm been cl~onen ,w n rofcmnrx:<br />

veloc~ity for the a7.imutal con~poncnt, w,(x, 2). 'I'ho preceding equations ~nnke it possi1)lo Lo pcrforrn<br />

cnlculntions for Inminar as well as for turbulent flows, it being necessary to introduce difircnt<br />

expression8 for the shearing stress at the wall in the latter cme (see ref. [R4] and Sec. XXllc).<br />

In some of the cases, it proved possible to evaluate the drag coefficient in addiLion to t,he t,nrning<br />

tnonwnt,, the former decreasing as the parameter mR/Um is increased. In this connexion, the papers<br />

I)y C. It. Illir~gwortl~ [54] and S. T. Clru and A. N. TilTbrcl [13] may nlso hc stdied. The approxilnate<br />

procedure conceived by H. Schlichting [98] was extenrlcd to compressible flows by .I. Y;rnlnga<br />

[125]. The preceding investigntions have bcen extcnded for laminar as well ns for t.nrl)ulent.<br />

tlows by theoretical and experin~ental investigation^ described in ucveral papers by ,Japanese<br />

authors [29n, 10, 01, 79, 801.<br />

l'rohlcn~s connected with laminar flow nbout a uphere rotating in a flnid at, resL IIGVO IICCII<br />

discussed by I.. Ilowarth [51] and S. I). Nigam [All. An extension to the case involving ellipsoids<br />

of revolut.ion wns provided by B. S. Fadnis p6]. Near tho poles, the flow is the same as<br />

on a rotating disk and near the equator it is like the one on a rotatin cylinder. The aecornpanyi~~g<br />

secondnry st re an^ causes fluid particles to flow into tho boundary yaycr near the poles, nntl out.<br />

of it at the equator. The rate of this secondary flow increases with increasing slenderness, the<br />

cquabrial area and peed of rotation remaining constant. However, the phenomena in the<br />

plnne of tho equator where the two boundary layers impinge on each other and are thrown<br />

outwards can no longer be analyzed with the aid of boundary-lnyer theory, el. W. 11. If. Banks [5a].<br />

Further theoretical and experimental investigations of t.his problem have been later under-<br />

taken by 0. Sawatzki [94] and by P. Dumsrgue et al. [21a]. Reference [94] describes n~edsure-<br />

rnenls d the torque exerted on a rotating sphere in the rango of Ibynolds number 2.105 < R <<br />

1.5 x 106 which goes far beyond the laminar regime. Tho invwtigntion of Ref. [21 a] included<br />

the vi~unlizntion of the spiral strenmlines near the wnll on n sphere nnd on cones of various in-<br />

cluded angles as they occur'in laminar flow.<br />

It has been observed that in axial turbomachines there may, under certain circumstances,<br />

appear an extended zone of dead fluid in tho whirl behind the row of stationary blades antl<br />

ncnr the hub. This phenomenon was described in great detnil by K. J3antmert and H. Klaeukens<br />

[5]. The origin of this dead-water area is conneckd wiLh the radial increase in prcssurr in Iho<br />

ontwnrtl direction which i~ due to the whirl. Owing to tho whirl the axinl pressure inerrme nrnr<br />

lhe huh in the bladelorn annulus behind the guides is much greater than at the outer wall. The<br />

influence of tho houndory layer is here only ciecontlnry. ALLonLion rn!ly, further, ho drawn Lo<br />

an invesbigotion duo Lo I

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