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Boundary Lyer Theory

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conclil.ion (4.14) plays n part wl~ich ia ein~ilnr tn 1.11~ no-slip condit.ion of n red fl~~id. 'Chc latter<br />

cnn be saLislic4 by Ihc solutions of 1.11~ Nnvicr-Stokcs eq~~etions I~ut not by those of Euler'a<br />

cquntio~~s. 'I'lw slowly-varying solnt,ion is trnnlngrr~~s In) tile frictionlcsn solution (ptrntinl flow)<br />

whicl~ f:rils to satisfy the no-slip contlil.ion. 7'11~ f~rst-vnrying solntion rcprcscnts Lhe counlr?rpart<br />

of tho bonndnry-lnycr ~oIuLion whicl~ ia delcrn~incd by t.ho prcscnm of viscosit.y; it clin'cn fron~<br />

zero only in n narrow zone near tho wall (boundary Inyer). It is to bo nokd that the second<br />

bonndnry condition (no slip at tho wall) can only be sal,inficd if this bountlnry-layer solution is<br />

a.dclwl, t,l111s mnking tho whole sol~~bion phy~icnlly red.<br />

This simple rxarnplc cxl~ibit,s thc sarnc matbcmstical Aaturcs M t.l~osc ch?usscd in 1,110<br />

prcrcding cl~u.plcr. It is, nrrrnrly, not pcrn~iasil~lc si~n rly In onlit tl~c viscou~ tern18 ill tlw<br />

Nnvicr-Stokm equation, wlmn performing the process or going over to t.he limit Tor very small<br />

viscosit.y (vrry I;irge llcynolrln n~~rnbrr). This wn only bc: clonc: in tile intrgrnl solnl.ion itxlr.<br />

We sha.ll tlcnionstratc latm in grcatcr c1cl:iil tht if, is not t1cc:c:ssary to rctain lhc<br />

Cull Navirr-St.olrcs eqnnt,ions for the process of finding the limit for R -+m. For<br />

lhc salte of n~athrmatical simplification il will provc possible to omit certain t.rrni~<br />

in it, pnrticnlnrly certain small viscous tcrnls. It is, however, important to note that,<br />

not all viscous trrma can bc ncglrctrtl. ns this woril~l depress tllc ordrr of tho Navier-<br />

Stolrrs rqnntions<br />

[l] Ackcrct, J.: Ubcr cxnkte J5sungen dcr Stokes-Navi~r- Glcicl~ungen inkomprrmihler 1Pliiimigkciton<br />

bci vcriin~lcrbn (:rr~~r,l~c~li~~~rtngc?~~.<br />

%1\;\11' 3, 259--271 (1952).<br />

[In] Apeelt. C. ,i.: 'l'hc ~trnrly Ilrtiv of a viscous flnid pat n circulnr cylindcr at Reynolds numbers<br />

40 and 44. Ikitisl~ AltC ItM 3175 (IWil).<br />

(Lh] Allen, D.N. 1)c G., m~ci So~~t.hwcll, 1t.V.: ltclaxation methods npplicd to deternline the<br />

mot,ion, in t,wo di~nm~iona, of R viscons flnid pnat n Bxetl cylinder. Q~mrt. J. Mecb. Appl.<br />

MnLIl. 8, 12!)-145 (1!)55).<br />

[lo] Coutnnccau, M., nnd Uo~lnrd, R.: 15xpcrirncntnl dckr~ninnt.ion of t.lw main fcnt,nrrs of the<br />

vinrn~~n flow in ...~. tho wakn of R circular cvlinder in 11uifor111 tra~~slation. Par1 I. Stendy now.<br />

~<br />

JFM 78, 231 -256 (1977j.<br />

[Id] (huta~~cenu. M., ~1r1 Ih~nrd, It.: RxprritnrnLal detcnnination of thc mnin fcnCuren of thc<br />

visco~~s flr~w in tbe wake of R circulilr cylinder in uniform trnnslation. Part 2. Unsbndy flow.<br />

.11W 79, 257- 272 (15377).<br />

[2] Ihmnis, S.C.K.. and GRII-ZII Chang: Nn~ncrical soI~~t,it)ns for stcarly flo~ past x circ~~lnr<br />

cylintlcr nt, I

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