A measurement technique of time-space characteristics of heat transfer to air has been developed using a thin conductive film and a high-speed infrared thermograph. In this work, a titanium foil of 2 m thick was used as a test surface, and measured temperature on it by employing an infrared thermograph of 120 Hz. The accuracy of the measurements was confirmed by comparing the heat transfer coefficient of a laminar boundary layer to that of a numerical analysis. In order to verify the applicability of this measurement technique to practical measurements, unsteady heat transfer on the wall of a turbulent boundary layer was examined. It was possible to restore the timespace distribution of the heat transfer coefficient up to 30 Hz in time and 4.5 mm in spatial wavelength by solving the heat conduction equations inside the wall, even though the heat transfer coefficient was low ( h = 10 – 20 W/mK). The results showed that the time-space behavior of the heat transfer was clearly revealed, which was reflected by the streaks formed in the near-wall region of the turbulent boundary layer. The statistical values of the turbulent boundary layer, that is, rms value of the fluctuating heat transfer coefficient and mean spacing of the thermal streaks, agreed well to those of previous data of DNS and experiments. INTRODUCTION Convective heat transfer generally has a nature of nonuniformity and unsteadiness, which is reflected by a three-dimensional flow near a wall. However, most experimental studies concerning the convective heat transfer have been performed in a time-averaged manner or using one-point measurements. This frequently results in poor understandings on the mechanisms of the heat transfer. Measurement techniques for time-space characteristics of the heat transfer have been developed using liquid crystal (Iritani et al., 1983) or using infrared thermography (Hetsroni and Rozenblit, 1994, and Nakamura and Igarashi, 2004, 2006), by employing a thin test surface having low heat capacity. However, the major problem of these measurements is attenuation of the temperature fluctuation due to the heat capacity of the test surface. Also, lateral conduction through the test surface attenuates the amplitude of the spatial temperature distribution. These attenuations are considerably large, especially for the heat transfer to air for which the heat transfer coefficient is low. The present author investigated the frequency response and the space resolution of the heat transfer from a test surface by solving heat conduction equations (Nakamura, 2007). Figure 1 (a) and (b) shows the upper limit of the fluctuating frequency, fmax, and the lower limit of the spatial wavelength, bmin, respectively, which are detectable using infrared thermograph, where h is fluctuating amplitude of the heat transfer coefficient and TIR0 is noise equivalent temperature difference (NETD) of infrared thermograph for a black body. If an extremely thin conductive film, as indicated in Fig. 1, is used as the heated surface, the unsteady heat transfer to air is observable up to f 50 Hz and b 1 mm (at Tw – T0 = 30C and h = 3 – 5 W/mK) by employing an infrared thermograph of nowadays ( TIR0 = 0.025C). In this work, the measurement technique using a thin conductive film and a high-speed infrared thermograph was applied to measure the unsteady heat transfer to air caused by flow turbulence. The attenuation due to the heat capacity and the lateral conduction was restored by solving the heat conduction equations inside the wall. NOMENCLATURE bc : cutoff wavelength in space bmin : lower limit of spatial wavelength detectable c : specific heat fc : cutoff frequency fmax : upper limit of fluctuating frequency detectable h : heat transfer coefficient l : wall-friction length = /u q : heat flux Re : Reynolds number based on momentum thickness T : temperature T0, Tw : freestream and wall temperatures TIR0 : noise equivalent temperature difference of infrared thermograph for a black body t : time u0, u : freestream and wall-friction velocities x, y, z : streamwise, vertical, and spanwise coordinates : thickness : thermal conductivity : kinematic viscosity of fluid : density of fluid Superscripts and Subscripts ( ) : mean value ( )rms : root-mean-square value