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242 XI. Axially nymmct.riral and tl~rrr-tli~r~rt~siot~al 1)onn~l:~ry Inyrra b. Approximate aolutiona for axinlly apmmctric boundary lnyer~ 243<br />
Fig. 11.8. Velocity distribr~bion in thc inlct port.ion of n pipe for the lnn~inar ca.se; mennurements<br />
perfornicrl by Nikuradac and quotrd from Pranc1t.l-Tiet.jen vol. TI. <strong>Theory</strong> dl10 to<br />
Scliillrr (901<br />
ltns prarf irally tlrcayctl al, :I clistancc of 40 pipe radii whcn thc Rcy~rol& nuntber<br />
has a value of R = 10:' This is in good agreement with experimental results.<br />
3. Rour~clnry layrra on rotating bodies of revolution. The simplest cxarnplc of<br />
e bounclary laycr on a rotaling hotly is tIi:~t considerod in See. Vb 11, namely the<br />
problem of a disk rotating in a fluid at, rest,. The fluid prticlcs which rotate with the<br />
boundmy laycr arc thrown outwards owing to the existence of ccntrifugal forces<br />
('centrifuging') anti are rcplaccd by part,icles flowing towards the boundary layer<br />
in an axial direction. Tlic casc of a disk of mtlius I< rot.nting with an angular vclocity<br />
o in an axi:~l sl.rc:~m of velocity U, :~lTords a simplc cxtcnsion of the previous<br />
problem. In thc lat,t.cr case the flow is govcrnctl by two parameters: thc Rcynoltls<br />
number and the rot,af ion pammetcr, U,/Rw, which is given by the ratio of frecst.rcam<br />
to tip vclocity. An cxact solution to the problem under consiclcration was<br />
given 11y Mi* D. M. Ilannah [46]t and A. N. Tiffortl 1.1 131 for tho case of laminar<br />
flow; IT. Sal~licl~ting and R. Truckcnbrotlt [98] providcd an approximate solution.<br />
E. Truclrcnbrotlt 11 191 investigated the case of turbulent flow. .Figure 11.9 cont,ains<br />
a plot of the torqnc coefficient,, C, = ilf/g e (2 R" in terms of the Reynolds<br />
numbcr and rotation parameter, U,/ll(u, obtained from such calculations. Here M<br />
clrnotcs the t,orque on thc leading side of the dislz only. When the disk rotatcs we<br />
may stmill assumc Ifhat separation occurs at the edge of the disk. 'l'he 'stn.gnant,'<br />
fluid Itchintl the clislr part,ly rot,n.tcs will1 thc,clislz and contributrs lit,l,le to the<br />
torcpc. Any such contribution has been lcft nt of account in (7, in Fig. 11.9.<br />
It is seen that Llie torque increases rapidly wi P 11 U, at constant angular velocity.<br />
t Arl.~tnlly rrf. 1381 solvm n rrl:rlr~l pro1,lrrn in wltirh the! cxtcrnal ficltl in t.l~:ct, rluc to '& source<br />
at infinity.<br />
Pig. 11.9.<br />
Morncnt cocllicient on<br />
a rotating disk in axial<br />
flow, aftor Gchlichting<br />
and Truckenbrotlt<br />
[98, 1 191<br />
Cnr - Mlf Q w' R';<br />
bf - torque on lcnrling sidc<br />
or dirk<br />
W4 2 4 6 WS 2 4 6 106 2 4 6 lo7<br />
Reynolds number R =g$<br />
Thc flow in a circular box provided with a rotating lid shows a markcd rcscmblance<br />
to that between two rotating dislts mentioned in Scc. V b 11. 7'11~ cnse<br />
of the flow inside the box was investigated in deLail by 1). Grohne [44] who discovered<br />
two peculiar features in it: First, the flow in the friction-free core in tlie<br />
interior of the box can only be determined by taking into account the inllncnrc of<br />
tlie boundary layers which form on the wall, in contrast to normal cascs whcn onc<br />
naturally nssymes that t,hc influence of tho flow in a bountlary layer resu1t.s at, most<br />
in a d.isplaccment. Secondly, the boundary laycrs arc unusual in that they join car11<br />
other. Siniilarly, in the arrangement oonsis1.ing of R rota1,ing channrl irivc?stligat,etl<br />
by IT. 1,udwieg [68], it is possiblc to discern two regions of flow when the spcxd of<br />
robation is sufficic?nt.ly high, ttamcly a fricd.ionlcss corc and bottndnry layrrs which<br />
form on the side walls and which givc risc t.o a secondary flow. 'l'hc t.hcory lcads<br />
to a large increasc of thc drag cocfficicnt which is dnc to rotation, ant1 this fact has<br />
been confirmed by experiment.<br />
Blunt bodies, sncli as o. a. a sphere or a slcrdcr body of revolution, placctl in<br />
axial streams, show a marked influcncc of rotation on dmg, as cvitlrncwl I)y tho<br />
measurements performed by C. Wicsclsbergcr 11231, ant1 S. 1~1t.h:~ndcr and<br />
A. Rydberg [69]. Fig. 11.10 contains a plot of thc drag cocfficicnt of n rotating<br />
sphcre in terms of the Rcynolds numbcr. It is secn that Lhc critical Rcynoltls<br />
number, for which the drag coefficient dcrrcascs abrnpt,ly, depends strongly on tlie<br />
rot,at.ion paramcler U,/Rw, and the same is true of the position of tltc point, of snp:~ration.<br />
The effect, of rotary motion on bl~c posilhn of the linc of 1aniirtn.r sc.pnr:~l.io~~ on<br />
a spltcrr is (l(;s(~il~cd by lhc grc~pli in ltig. I I .I I ; 1,Itc (IILIJL ror it IIILVO INWI ~ X ) I I I ~ ~ I I I ~ I ~ I I<br />
by N. E. lloskin [50]. When the rotatmion para.mctcr 11:~s nl,tdinrtl t,hc vn111c:<br />
Q = w R/[J, = 5, the line of sepnm.t,ion will have moved by about lo0 in 1,hc upst,rean~<br />
direction, as compared with a sphere at rcst. 'l.'hc physicnl ren.son for this<br />
bef~aviour is connected with the centrifugal forces &ding on t,hc fluit1 parLiclcs rolat,ing<br />
wit,]i the body in its bour;tlary layer. Thc crt~trifngal forces have tlic sn,mc rni~t n.s an<br />
atltlit.ionnl pressure gratlirnt dircctd towards t,hc plnne of I,ltc erlun.t,or.