1991
DOI: 10.2514/3.46114
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Heat transfer measurements from a smooth NACA 0012 airfoil

Abstract: Local convective heat transfer coefficients were measured from a smooth NACA 0012 airfoil having a chord length of 0.533 m (21 in.). The measurements were made both in flight on the NASA Lewis Twin Otter icing research aircraft and in the NASA Lewis icing research tunnel (IRT). Flight data were taken for the smooth airfoil at Reynolds numbers based on chord in the range 1.24 X 10 6 to 2.50 x 10 6 and at various angles of attack up to 4 deg. During these flight tests, the freestream velocity turbulence intensit… Show more

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Cited by 27 publications
(18 citation statements)
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“…A NACA 0012 airfoil was used for this testing as it is well characterized for ice accretion from extensive testing in supercooled liquid water (e.g. [11,12]) thereby eliminating the need to characterize certain aspects of the airfoil. The ice shapes were generated across a series of four different flow conditions where the relative humidity in the plenum was the primary parameter varied.…”
Section: Introductionmentioning
confidence: 99%
“…A NACA 0012 airfoil was used for this testing as it is well characterized for ice accretion from extensive testing in supercooled liquid water (e.g. [11,12]) thereby eliminating the need to characterize certain aspects of the airfoil. The ice shapes were generated across a series of four different flow conditions where the relative humidity in the plenum was the primary parameter varied.…”
Section: Introductionmentioning
confidence: 99%
“…The non-dimensional radial location (r/R) was described by the ratio of the distance to the placed RTD by the tip radius of the blade. Due to experimental limitations, the RTDs were placed on the nose of the leading edge (S/c = 0), a point known to show some of the most elevated heat transfer rates [43,52]. More chordwise locations are scheduled for testing in the future.…”
Section: Heating Elements and Rtdsmentioning
confidence: 99%
“…The air properties vary with temperature. Therefore, a reference temperature (T f ) was chosen to estimate those properties, similar to [43]. According to [54], the equation can be applied for a flow where V ∝ is a constant and the temperature does not vary markedly in the boundary layer.…”
Section: Convective Heat Transfermentioning
confidence: 99%
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“…The two temperatures are shown in dashed lines and correlate with each other very well. The chart on the bottom is the calculated heat transfer coefficient comparison from Equation 11.…”
Section: Figure 6 Sample Heat Transfer Time History Datamentioning
confidence: 99%