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Boundary Lyer Theory

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714 X X I I I. 'hrhulcwt. I)oc~ntl:~.ry I:rycrs in conq)rcrrsiblc flow<br />

flow, rxpcrirnr~~ts showing tltat on the avcragc its value placcs itaelf between 0.875<br />

ant1 0 88 (see lj'i'ig 17 31). 'I'hc diagram in l'ig. 23.5 rcproduccs 1,. M. Mack's [56]<br />

comparison of valucs of the rrcovcry fartor, r, measurcd on concs at cliffcrcnt Mach<br />

numhrrs and at cliffcrcnt Itrynoltls numbrrs In order to rstimate the cffcct of<br />

Pr:tntlt,l nurulwr, many rtutllors quote thc formula<br />

whic:l~ yioltls r .-I 0.896 at. P :-: 0.72. It is rtlso possildc t.o obtain this csthatc thcorcti-<br />

oally, in a mallncr analogous to that used I,r thc crtlculntion of tltc cocfficiont of<br />

11eaL transfer. For this I)urpost? it is ncccssary to start with the cncrgy equation<br />

(23.1 1 (:) ant1 10 irlclutle Lhc cffoots of Cllc molecular and of tho turbulcnt transfer<br />

mechanisms in aocortlancr! whicll the hypot.hcsis contraincd in eqn. (23.14). Proceeding<br />

in this way, .J. C. Rotta [81] obtaincd the cquation:<br />

Tltc quantity h is a function of the raLio PIP, and accounts for, like the quantity a<br />

in cqn. (23.20), tho procwscs taking place in the laminat' sublayer. It is given by the<br />

intrgral<br />

Wind lunncl 1 Mm 1 Typo of pone<br />

I<br />

k~,ercirca<br />

(:AI.CIT 5 x G In.<br />

Aatm I x 3 lt No. 1<br />

JI'L I8 x 20 in.<br />

I ' 18 x 20 in.<br />

J I I?( x 20 in.<br />

J I 12 x 1% in.<br />

I , 12 x 12 in.<br />

2.18 10' wood<br />

6.0 20" ccrnrnlc<br />

2.0 PO' l~olluw; slrcl<br />

4.60 5" nl~rcglnss<br />

I.o:l 13' lucitx<br />

4-50 13" llrcitc<br />

1.W 13" lf~cilc<br />

2.54 10" lllcitr<br />

c. Influcncc of Mach nunher; laws of fricbion 715<br />

Numerical values have bcen incluticd in Table 23.1. The factor 13 dcpcnds on P, and<br />

somewhat on dc,'/2 . According to Rotta, we may take<br />

When the turbulrnt I'mndtl number varies over the thicknrss of thc bouutlary<br />

layer, it is necessary to insert into eqn. (23.24) the value assumed by it at the wall.<br />

Whcn the Pmndtl n~lml)er, P, as well as the turbulcnt Prantltl number, P,, differ<br />

from nnity, it is worth noting that, normally, eqn. (13.21) givcn in Chap. XTII for<br />

laminar bountlary layers constitutes a usable approximation for the tcmpcmt~lrr<br />

distribution in a comprcssiblc turbulent boundary layer. 13. SchulCz-Jnncl~ 1!15]<br />

dcvelopcd n procedure for the calculation of temperature distributions in turbuicnt<br />

comprcssible boundary layers.<br />

c. Infl~~enee of Mnch nun~ber; lnws of friction<br />

To date, the calculation of turbulcnt boundary laycrs in inconl pressiblc flow<br />

has not developed to a point where it could be classccl as bcing morc than a semiempirical<br />

theory. It is, therefore, not surprising that the same remark applies to the<br />

cnlc~tlation of comprcssil)lc tur1)ulcnt boundary layers. In tho rnsc of incomprcssil)lr<br />

turbulcnt bounclwy laycm a starting point is proviclctl by tllc hypothcscs whicll wc-rc<br />

tliscusscd in the prcccding chnptcrs, narnrly by l'rnntltl's mixing-lcrlgt.11 Ilyl~otlw~is,<br />

by von Kilrmh's similarity rule or by Prandtl's universal velocity-distribution law.<br />

The authors of numerous contemporary papers have cndcavourcd to create a semiempirical<br />

theory of comprcssiblc turbulcnt boundary layors by transposing thcsc<br />

hypotheses and by adapting them to thc compressible case. This ncccssitatcd thc<br />

introduction of additional ad hoc hypotheses. In the absence of detailed investigations<br />

into the mechanics of compressible turbulent flows, thc transposition of thc semiempirical<br />

theories of turbulent flows from the incompressible to tho cornprcssible<br />

case involves a good deal of arbitrariness.<br />

Prom the practical point of vicw, thc tlimcdtics incrcnsc bccnusc, on tl~c one<br />

hand, there arc two additional pamrnetcrs- thc Mach numbcr, A&,, of thc: froc<br />

stream and the temperature, T,, of tllc solid surface- which influence the flow, and,<br />

on trhe other hand, tile available experimental results are not cntircly frcc of contmdictions.<br />

Tllrcc mcthotls should bc singlcd out from among tl~c numcrous propos:ds<br />

for handling the problem, bccause they havc bcen employcd parlit:ularly freq~lentIy:<br />

(1) Introduction of a reference temperature for the density and viscosity of the gas.<br />

(2) Application of PrantlLl's mixing length hypothesis or of von Kitrmbn's similarity<br />

hypothesis.<br />

(3) Transformation of the coordinates.<br />

Over and above, the litcrature of thc subjcct contains expositions of mc4lotls<br />

which cannot be classified under any onc of the thrcc proceding hcdding~. In an<br />

impressive comparison, D.R. Cllnpmnn and R.11. Kcstcr [I I] brought to thc forc<br />

the large diffcrcnces which result when cliffercnt methods arc usctl to calculat~c skin<br />

friction (cf. [30]). An extensive comparison betwcen twcnty cliffcrcnt ~omput~ational<br />

schemos and cxisting, expcrimental rcsults was carried out by D. R. Spnlding and<br />

S. W. Chi [89].

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