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Pohlhausen

Norris and Spofford [Tron.s. Am. Soc. Mech. Eng., 64, 489 (1942)] correlate their results for air by the dimensionless equation of Pohlhausen ... [Pg.564]

For turbulent flow on a rotating sphere or hemisphere, Sawatzki [53] and Chin [22] have analyzed the governing equations using the Karman-Pohlhausen momentum integral method. The turbulent boundary layer was assumed to originate at the pole of rotation, and the meridional and azimuthal velocity profiles were approximated with the one-seventh power law. Their results can be summarized by the... [Pg.178]

Karman-Pohlhausen method predicts a time for complete solidification which is too small by more than 40%. [Pg.131]

Pohlhausen, 1911 [1] solved these equations first, whereas Schmidt and Beckmann, 1930 [2] solved them for Pr = 0.733 in 1930. Ostrach, 1953 [3], solved the same equations for the range 0.01 to 1000. For free convection laminar boundary layer on a heated vertical plate in that range of Pr, the velocity and the temperature distributions are shown in Figs. 9.2 and 9.3, respectively. [Pg.145]

E Pohlhausen. Der Warmeaustausch Zwischen Festen Korpen und Flussigkeiten mit kleiner Reiburg and kleiner warmeleitung, Z Angew Math Mech, Vol 1 115, 1911. [Pg.158]

The relationship of Pohlhausen was used for the heat transfer in the separation space (22) ... [Pg.62]

Pohlhausen (P4) in 1921 presented the direct solutions of the convection equations for the laminar boundary layer on the upstream portion of a flat... [Pg.248]

In the integral condition (3.165) for momentum the velocity profile is approximated by a polynomial first suggested by Pohlhausen [3.6], such that... [Pg.315]

These equations were first solved by Pohlhausen [3.48] for air with a Prandtl number Pr = 0.733 by series expansion and later numerically by Ostrach [3.47] for a wide range of Prandtl numbers, 0.008 35 < Pr < 1000. Fig. 3.45 illustrates the normalised velocities in the form... [Pg.382]

Pohlhausen, E. Der Warmeaustausch zwischen festen Korpern und Fliissigkeiten mit kleiner Reibung. Z. Angew. Math. Mech. 1 (1921) 115-121... [Pg.661]

Pohlhausen, E., Warmeaustausch zwischen festen Korpern und Flussigkeiten mit kleiner Reibung und kleiner Warmeleitung, Zs. angew Math. Mech. (ZAMM), Bd. 1, S. 15, 1921. [Pg.364]

The simplest situation, that of the transport from a flat plate at zero incidence to a flowing stream, was considered in Section 2.3. The solution to the problem of ranss transfer with a constant surface composition based on Pohlhausen s bent transfer solution cen he written in the formt... [Pg.106]

Pohlhausen [2] utilized the Blasius coordinate system and velocity distribution to evaluate the convective heating processes within the constant-property boundary layer on a flat plate. He solved two problems ... [Pg.442]

The latter is the plate thermometer or adiabatic wall problem. Eckert and Drewitz [3] showed that the general problem of heat transfer to a uniform-surface-temperature plate in constant-property high-speed flow is merely the superposition of the two Pohlhausen solutions. [Pg.443]

The local Stanton number found by Pohlhausen is represented very well by... [Pg.443]

FIGURE 6.7 Effects of viscosity changes across a laminar liquid boundary layer on surface shear and heat flux—reference shear from Blasius solution with free-stream properties, reference heat flux from Pohlhausen solution with wall properties [7]. [Pg.448]

It is also possible to employ the von Kdrman-Pohlhausen integral method (see, e.g.. Been, 1998, pp. 353-356) to develop a starting concentration profile for reactant A in the inlet region, subject to the five requirements outlined above. This method conserves mass over the thickness of the mass transfer boundary... [Pg.622]

Solving the system of equations for conservation of energy, momentum, and mass for the longitudinal flow past a plate at constant wall temperature results in the following equation for the heat transfer coefficient (Pohlhausen 1921) ... [Pg.197]

Millsaps, K., Pohlhausen, K. (1952). Heat transfer by laminar flow from a rotating plate. [Pg.621]

In 1963, Barua assumed that the flow through curved pipe consisted of an inviscid core plus a thin boundary layer, the flow in the core lay in planes parallel to the plane of symmetry he used Pohlhausen momentum integral method to solve the... [Pg.386]

Ito [95] improved the boundary layer model of Barua [91] and used Pohlhausen integral method to solve it. He gave the following correlation. [Pg.387]

Pohlhausen (Kl) was able to show that the relation between the hydrodynamic and thermal boundary layers for fluids with Prandtl number >0.6 gives approximately... [Pg.372]


See other pages where Pohlhausen is mentioned: [Pg.174]    [Pg.99]    [Pg.128]    [Pg.128]    [Pg.129]    [Pg.130]    [Pg.130]    [Pg.655]    [Pg.657]    [Pg.249]    [Pg.292]    [Pg.289]    [Pg.444]    [Pg.446]    [Pg.772]    [Pg.25]    [Pg.125]   
See also in sourсe #XX -- [ Pg.655 ]




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