NASA NACA-TR-793-1944 Experiments on Drag of Revolving Disks Cylinders and Streamline Rods at High Speeds《在高速下 旋转盘 汽缸和流线型棒条阻力的实验》.pdf
《NASA NACA-TR-793-1944 Experiments on Drag of Revolving Disks Cylinders and Streamline Rods at High Speeds《在高速下 旋转盘 汽缸和流线型棒条阻力的实验》.pdf》由会员分享,可在线阅读,更多相关《NASA NACA-TR-793-1944 Experiments on Drag of Revolving Disks Cylinders and Streamline Rods at High Speeds《在高速下 旋转盘 汽缸和流线型棒条阻力的实验》.pdf(18页珍藏版)》请在麦多课文档分享上搜索。
1、REPORT No. 793 EXPERIMENTS ON DRAG OF REVOLVING DISKS, CYLINDERS, AND STREAMLINE RODS AT HIGH SPEEDS By TODOEE TFLBODORBN and AE- RDQIER SUMMABY An experimentid investigation concerned pimarily with the e therefore u- u, -=fa U, (z) 367 Provided by IHSNot for ResaleNo reproduction or networking perm
2、itted without license from IHS-,-,-. I . .- 368 REPORT NO. 793-NATIONAL ADVISORY COMhLT?TEE FOR AERONAUTICS This quite remkable relationship, which has been generally confirmed by Nikuradse, Wnttendorf, and others (references 5 to 7), implies a similarity in the turbulenbfield pattern nmay from the
3、molls at all Reynolds numbers. The basic reason for this similarity remains unknown. It follows ram ssumption (2) that near the wall =I K log $+Constant where l/ is the constant of proportionality. (Natural logarithm haa been used throughout except where othenvise indicated.) Since u= Ua at y=6, thi
4、s relation reduces to This logarithmic relationship holds to a certain value c of the signi6cnnt pameter a (see fig. l), where c=ka vith k a constant. The value of 1-k is only a small fraction, so that the point c will be relatively close to the mall. The velocity in the center of the pipe is theref
5、ore given as the sum of three exprssions, that is, For the lnminar sublayer ua 6 u. E=a - and the equntion mny be rewritten as la =a+; log E+“* whero and 1 C,=a- log a K c;= f I! +-log; c (a): : The const.ant C1 is equal to the nondimensiond velocity measured on the logarithmic velocity profile when
6、 this curve is extrapolated to y=L, and the constant Cr is the exw velocity in the center of the pipe 8s compared with that of the logarithmic line extended to y=a. (See fig. 1 .I When these constants axe combined, the following general relation is obtained: qy =“+; la log E The application of this
7、theory to caw other than circular pipes is restricted to geometric configurations given by a single parameter. It is interesting to observe that both Cl and 1/ are universal constants resulting from tho second assumption-namely, that the flow near a wall is a function of the distance from the wd onl
8、y The second constant C; which gives the excess velocity na compsred wit11 tho logarithmic distribution at a reference point, the locntion of yhich depends on the geometric dimensions involved, is not a universal constant but is dependent on the configurntion nnd the choice of reference length. The
9、effect of surface roughness may be treated in a similnr manner. If the roughness parameter e/L js less than a cerhin ma-dtude, there is obviously no effect at d. This vnlue of a/L is found experimentally to be 3.3. 3.3, U UT - or The velocity distribution is .exactly ns if there were n laminar layer
10、 present of a thickness 6c3.5 or ns if the length 1 1 L were - E- When L the velocity dishibution no 3.3 longer changes with an increase in Reynolds number R. It seems, therefore, that the distance from the wall of the innermost disturbance, or the mean value of the thickness Q.“ Provided by IHSNot
11、for ResaleNo reproduction or networking permitted without license from IHS-,-,-DRAG OF REVOLVING DISKS, CYLINDERS, AND S!CREAMLIAW RODS AT HIGH SPEEDS 369 of the laminnr layer, is of the order of three to four times the height of the irrcgularitim or the grain size E. This fact is not inconsistent w
12、ith the physical interpretntion. The quantity U therefore, (See reference 3, p. 142.) and, finally, with R and CD referring to the mean velocity, where With 0=5.5 and =0.4, P, 0.4 This value is not accurately established, as the various authors seem to differ. DRAG OF FLAT PLATES In order to obtnin
13、the drag formula for flat plates, n calculation similar to the von KBrmh-Prandtl treatment for pipes may be performed. The velocity deficiency Auk given by the relation where UTm is a mean value between 0 and 2, the distance along the plate. The missing momentum may be mitten as or where U is the st
14、renm velocity and 61 is a significant length giving the thickness of the boundary layer. Rewritten, this equation becomes or, by virtue of the similarity law, Since the momentum is given directly as the following identity is obtained: or Using the logarithmic deficiency relation gives for C5 the val
15、ue I/., or 2.5, and for c6/c5 the value 2/, or 5; thus Provided by IHSNot for ResaleNo reproduction or networking permitted without license from IHS-,-,-370 REPORT NO. 703-NATIONAL ADVISORY COMMITTEE FOR AERONAUTICS By use of the von KhBn-Prandtl treatment, the stream velocity is obtained in essenti
16、ally the same form as for pipes. With small adjustments, therefore, By use of the expression for for the full length I, With the subscripts m and z referring to mean and local values, respectively, for the length x, or Therefore where BOUNDARY RELATION FOR REVOLVING DISK8 The moment coef6cient is de
17、fined as The moment may also be mitten M=2p (24urup. dy where u, is the variable radial velocity and ut is the tnngen- tial velocity, from which or !=constant a The drag formula then reads A similar result was obtained by Goldstein in referonce 4. . TESTS AND RESULTS Tests on disks, cylinders, and s
18、treamhe rods wore con- ducted to determine drag or moment coefficionts. For tho cylinder the two coefficients are equivalent; for tho disk and the rod it is more convenient to employ tho momont coo5- cient, which can be msasured directly. In order to oxtond the range of Mach number, several tests WO
19、TC conducted with Freon 12 or Freon 113 as the medium. Tho test results obtained are of technical interest bccause mmo of the data, particularly for the high Mach numbor rango, were obtained for the first time. It may be pointed out that many of the earlier tests on revolving disks and, in particula
20、r, on revolving cylinders more conductod on n rather amah scale and in a limited range of Roynolds num- ber. It may be notrd that a considerable mngo of Roynolds number is generally needed in order to confirm with su5- cient reliability a particular theoretical formula. For instance, it may be impos
21、sible to obtain a meosurable difference between logarithmic or power formulas if a short range of Reynolds number is available. This mattor of distinguishing between the various types of formulas is of theoretical interest. EXPBRIMENTB ON REVOLVING DISKS The moment coefficient is defined as M Cx=, 7
22、Pwa6 This definition corresponds to the one for laminar flow on a revolving disk given by von K6rmfin in referenco 1 as: Cdd = alR-In where CLULz E=- 0 Provided by IHSNot for ResaleNo reproduction or networking permitted without license from IHS-,-,-DRAG OF REVOLVING DISKS, CYLINDEEtS, AND STREAMLIN
23、E RODS AT HIGH SPEEDS -f. 0 %2, 34 371 won Kdrms lamnor-ffow formula, o 24-1k-diam. this value was later adjusted by Cochran (see reference 8, vol. I, p. 112) to ul=3.87. If this corrected value OI al is inserted, the formula for laminar flow rends Ck= 3.87R-“ The turbulenbflow formula as given by v
24、on K:=0.03, also used for the preceding os- perimenhl results shown in figure 8. It is verified that tho critical Reynolds number depends on the grnin size only, and it is further shorn that the slope of the drag curvo beyond the critical Reynolds number is a function of the density. A saturation co
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