1966
DOI: 10.1016/s0065-2717(08)70050-9
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Heat and Mass Transfer in Turbulent Boundary Layers

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Cited by 13 publications
(9 citation statements)
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References 43 publications
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“…In Fig. 6, the present results are compared to correlations for the film cooling effectiveness in the near-slot region from Lefebvre (1972, 1973), who summarized results from Stollery and El-Ehwany (1965), Leont'ev (1966), Whitelaw (1967) and Bradbury (1967). In case of the blowing ratios M = 1.6 and M = 3.39, the present results agree excellent with Ballal's and Lefebvre's correlation.…”
Section: Film Cooling Effectivenesssupporting
confidence: 77%
“…In Fig. 6, the present results are compared to correlations for the film cooling effectiveness in the near-slot region from Lefebvre (1972, 1973), who summarized results from Stollery and El-Ehwany (1965), Leont'ev (1966), Whitelaw (1967) and Bradbury (1967). In case of the blowing ratios M = 1.6 and M = 3.39, the present results agree excellent with Ballal's and Lefebvre's correlation.…”
Section: Film Cooling Effectivenesssupporting
confidence: 77%
“…Температурное поле гильзы цилиндров [3] назначали согласно экс-периментальным данным, полученным в режи-ме номинальной мощности двигателя. Допол-нительно задавали значения коэффициентов теплоотдачи и температуры охлаждающей жидкости в полостях моноблока [4,5]. Послед-нюю на входе в дизель принимали равной 60 °С, а на выходе из него -80 °С как максимально допустимую температуру [6,7].…”
Section: таблицаunclassified
“…5, где желтым цветом обозначены граничные Рис. 5 Данный характер деформации обусловлен тем, что моноблок нагрет неравномерно, так как со стороны выпуска температура значительно выше, чем со стороны впуска, это ведет к более интенсивному расширению материала с более нагретой стороны и, как следствие, к изгибу.…”
Section: рис 2 конечно-элементная модель моноблокаunclassified
“…ii'ir eli- Under stationary conditions a gas mass flow rate with the temperature T can be established through the porous disc (Afgan and Leontiev, 1994), (Martins et a], 1994). It is known, (Hartnet and Eckert, 1957), (Kutateladze and Leontiev, 1964) and (Leontiev, 1966) that at a specific gas mass flow rate through the filament, the boundary layer of the gas flowing over the porous filament is blownoff, resulting in the convective heat transfer at the surface to become practically equal to zero. In the case of an external flow over a porous surface with a laminar boundary layer developing over it, the critical value of the blow-off parameter is j.,o Reg = C…”
Section: Basic Principlementioning
confidence: 99%
“…For the case of a turbulent boundary layer, the direction of the flow relatively to the porous surface is not important, but a more complex expression is required to determine the critical blow-off gas (BOG) mass flow rate as a function of the external flow characteristics. A detailed discussion on this topic can be found at reference (Leontiev, 1966). A synthesis of this whole theory, focus on the present application can be found at (Martins et al, 1998b).…”
Section: Basic Principlementioning
confidence: 99%