2003
DOI: 10.1016/s0017-9310(03)00291-6
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Heat transfer in turbulent separated flows in the presence of high free-stream turbulence

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Cited by 60 publications
(30 citation statements)
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References 25 publications
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“…The temperature profile minimum (caused by the flow separation) as well as the temperature maximum (caused by the flow reattachment) has moved further towards the diffuser inlet in the case of the non-rotating diffuser. Another important feature is the reduced length of the separated flow region (i.e., the length between separation and reattachment point) as the Re number increases; according to the results of other experiments conducted by Obi et al [14] and Terekhov et al [18], this phenomenon should be connected with the higher free-stream turbulence at higher Re numbers. Thus, the distance between separation and reattachment point of the non-rotating diffuser is (by Fig.…”
Section: Resultsmentioning
confidence: 87%
“…The temperature profile minimum (caused by the flow separation) as well as the temperature maximum (caused by the flow reattachment) has moved further towards the diffuser inlet in the case of the non-rotating diffuser. Another important feature is the reduced length of the separated flow region (i.e., the length between separation and reattachment point) as the Re number increases; according to the results of other experiments conducted by Obi et al [14] and Terekhov et al [18], this phenomenon should be connected with the higher free-stream turbulence at higher Re numbers. Thus, the distance between separation and reattachment point of the non-rotating diffuser is (by Fig.…”
Section: Resultsmentioning
confidence: 87%
“…Diffusion coefficient D 1 Diameter of inlet tube D 2 Tube diameter behind expansion ER = (D 2 /D 1 ) 2 Degree of tube expansion S = (D 2 − D 1 )/2…”
Section: List Of Symbols Dmentioning
confidence: 99%
“…A sudden expansion in the tube or separated flow behind a back-facing step is the subject of numerous experimental and theoretical studies [1][2][3][4][5][6][7][8][9][10][11][12][13][14][15][16][17][18][19][20]. Interest in this issue, together with important practical applications, is primarily caused by the fact that this problem is a classic one and is the most studied of a wide range of separated flows.…”
Section: Introductionmentioning
confidence: 99%
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“…1). The stepped nose of the model approximately 100 mm long formed a turbulent boundary layer approximately 10 mm thick with the velocity distributed as 1/7 [11]. Two models of identical size were used to measure the thermal and dynamic characteristics of the model.…”
mentioning
confidence: 99%