Abstract

4 is, first of all, also relatively simple, involving at most a numerical quadrature. (Indeed, the quadrature takes into account, in a way, the previous history of the boundary layer.) Moreover, the formula of Morduchow and Clarke holds both for incompressible flow and for compressible flow with zero heat transfer, and the calculations are virtually as simple for the latter case as for the former. This is evidenced by the ease with which the cases in Ref. 1 were calculated by this means. With regard to accuracy, considering first incompressible flow, it hardly can be denied that the agreement of the formula of Morduchow and Clarke with essentially exact solutions is very good1 and certainly is sufficient for practical purposes. For example, the values of £ s for the case u\/u^ — 1 — t;n are everywhere within 2.5% of Tani's values.1. 3 Such agreement is especially noteworthy since the method of Ref. 4 is entirely self-contained and makes no use of any known exact solutions for either incompressible or compressible flow. As regards compressible flow, Curie states that the present authors' agreement with Stewartson's values of f s vs Mm for Ui/Uoz = 1 — £ simply means that both sets of values are in 30 or 40% error at Mm = 4. He bases this on the value fs = 0.045 (±10%) for Mm = 4, reported by him 5 and obtained by Mathematics Division, National Physical Laboratories. No details at all are given of how this computation, which is far from routine and involves, for example, a singularity at the separation point (cf., the machine calculation for the incompressible case6), was carried out. There have been some other purportedly fairly accurate calculations of this case which do not agree with the National Physical Laboratories value. These results, which are discussed below and shown in Table 1, indicate that it appears rather premature at present to infer that the present authors' results have such a large quantitative error at Mm ^ 4. Stewartson's calculations7 are based on the application of his well-known transformation to obtain a corresponding incompressible flow and then the calculation of the latter flow by means of Howarth's polygonal method.8 Tani9 used a two-parameter method based on the momentum and energy integral boundary layer equations. His results are seen to be in good agreement with the present authors' (or Stewartson's) for all Mach numbers calculated, especially if corrections for Prandtl number and viscosity are considered. Tani's results are based on the Sutherland viscosity-temperature relation and on a Prandtl number Pr of 0.72. According, for example, to Gadd, 10 the effect of changing Pr from 1 to 0.72 is to move the separation point downstream by about 7 or 8% at Mm = 4, with a similar effect at other Mach numbers. If this effect is considered at Mm = 4, it is seen that Tani's results at M^ = 4 (and at other Mm) will be brought still closer to the present authors'; a correction 10 for nonlinearity of the p, — T relation probably also would move Tani's values still closer. As previously indicated,1 Wrage11 has recently calculated this case by extending Gortler's series method to compressible flows, in conjunction with a finite-differe nce method and an electronic computer. Table 1 shows that Wrage's results are substantially similar to the present authors'; the largest deviation appears to be at Mm = 6 (viz., about 13%), but, interestingly, Wrage's results come still closer at Mm = 10. An application of Stewartson's transformation to Thwaites' method12 leads to results10 quite similar to the present authors'. (A perusal of the literature has indicated that there have been a variety of still other calculations of £ s for the problem treated here, and some of them deviate considerably at various Mach numbers from the results in Table 1. However, in each such case the method used was admittedly very approximate and gave appreciable error at Mm = 0. Moreover, the results of these methods for various Mm deviated considerably from one another, without the consistent agreement for all Mm shown by the various results in Table 1.)

Talk to us

Join us for a 30 min session where you can share your feedback and ask us any queries you have

Schedule a call

Disclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.